JP6368129B2 - How to remove radioactive material - Google Patents
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本発明は、陽電子放射断層診断装置において診断薬として用いられる18F標識化合物を合成する合成室で発生する放射性物質を効率的に除去する方法に関する。 The present invention relates to a method for efficiently removing radioactive substances generated in a synthesis room for synthesizing an 18 F-labeled compound used as a diagnostic agent in a positron emission tomography diagnostic apparatus.
医療機関では、癌発生部位の早期発見、早期治療の要求から、腫瘍に集まる性質を持つ化合物の一部の元素を放射性核種に置き換え、患者に投与し、体外から放射線を計測し、腫瘍部位を特定する放射線診断(インビボ診断)が行われている。近年、患者の不要な被ばくを避けるために、半減期が短く物質透過性の高いγ線を持つ放射性核種で標識した化合物が求められ、1崩壊(β+壊変)につき511keVのγ線を反対方向に2本放出する、ポジトロン放出核種による標識化合物が用いられている。この標識化合物を用いた診断装置は、陽電子放射断層撮影装置(PET:Positron Emission Tomography)と呼ばれ、小さな腫瘍部位まで発見できることから、多くの医療機関で設置されている。 In medical institutions, due to the need for early detection and early treatment of cancerous sites, some elements of compounds that gather in tumors are replaced with radionuclides, administered to patients, radiation is measured outside the body, and tumor sites are identified. Specific radiodiagnosis (in vivo diagnosis) is performed. In recent years, in order to avoid unnecessary exposure to patients, compounds labeled with radionuclides having a short half-life and a high permeability to gamma rays have been sought, and 511 keV gamma rays per decay (β + decay) are directed in the opposite direction. Two labeled compounds with positron emitting nuclides are used. A diagnostic device using this labeling compound is called a positron emission tomography (PET), and can be found even in a small tumor site, and is installed in many medical institutions.
標識化合物に主に用いられる放射性核種は、11C、13N、15O、18Fなどである。これらの核種は、その半減期(寿命)の短さから、主に実際に診断を行う医療機関において、陽子や重陽子を加速する超小型サイクロトロンによって製造される。製造後、これら核種は、自動的に合成装置に送られて医療用診断薬(標識化合物)となる。標識化合物は、純度や投与量の調整後、検査室で被検者に投与される。腫瘍細胞の糖分の消費が高いことを利用した多糖類、18F FDG(フルオロデオキシグルコース)が近年良く用いられている。18Fは、水(H2O)の構成原子である酸素を非放射性同位体である18Oで置き換えたH2 18O(ターゲット)にサイクロトロンで加速した陽子を照射して得られる。18F FDGは、合成室と呼ばれる小さなクリーンルームに置かれた専用の自動合成装置でフッ素化といわれる工程を経て合成される。 Radionuclides mainly used for labeling compounds are 11 C, 13 N, 15 O, 18 F, and the like. Because of their short half-life (lifetime), these nuclides are produced by ultra-small cyclotrons that accelerate protons and deuterons mainly in medical institutions that actually perform diagnosis. After production, these nuclides are automatically sent to a synthesizer to become a medical diagnostic agent (labeled compound). The labeled compound is administered to the subject in the laboratory after adjusting the purity and dose. In recent years, a polysaccharide, 18 F FDG (fluorodeoxyglucose), which utilizes the high sugar content of tumor cells, has been frequently used. 18 F is obtained by irradiating protons accelerated by a cyclotron to H 2 18 O (target) in which oxygen which is a constituent atom of water (H 2 O) is replaced by 18 O which is a non-radioactive isotope. 18 F FDG is synthesized through a process called fluorination by a dedicated automatic synthesizer placed in a small clean room called a synthesis room.
自動合成装置は、ヘリウム漏洩検出器などにより漏洩検査がなされている。しかし、試薬、器具及びイオン交換樹脂カラムなどの交換・接続時に接続部分から漏洩する可能性がある。また、反応系内のガスを系外に放出する際に含まれる未反応の18Fはソーダライム等の吸収剤により除去されるが、使われている吸収剤の劣化が原因で18Fが放出されることがある。漏洩する容量が微小であっても、放射線量としては非常に多い。製造を途中で中止した場合、放射能の減衰を待って分解・洗浄等を行わなくてはならないため、その日のうちに再度製造・合成を行うことは困難である。また、漏洩量が多く、排気中の放射性物質濃度が上がり、関係法令で定められた規制値を越えると、法令違反扱いとなり、しばらく放射性医薬品の製造、診断業務を中止しなければならず、患者に迷惑をおよぼす。そのため、合成室内に設置された自動合成装置から僅かな漏洩で生じた汚染された空気は、合成室に接続するダクトによって放射線施設の排気浄化設備に運ばれ、そこで粒状活性炭フィルターやHEPAフィルターまたはULPAフィルターにより浄化される。 The automatic synthesizer is inspected for leaks with a helium leak detector or the like. However, there is a possibility of leakage from the connection part when the reagent, instrument, ion exchange resin column, etc. are exchanged or connected. Moreover, unreacted 18 F contained when the gas in the reaction system is released to the outside of the system is removed by an absorbent such as soda lime, but 18 F is released due to deterioration of the used absorbent. May be. Even if the leakage capacity is very small, the radiation dose is very large. If the production is stopped halfway, it must be disassembled and washed after waiting for the decay of radioactivity, and it is difficult to carry out production and synthesis again within the same day. In addition, if the amount of radioactive material in the exhaust gas is high and the concentration of radioactive substances in the exhaust gas is increased and exceeds the regulation values stipulated by related laws and regulations, it will be treated as a violation of laws and regulations, and the manufacturing and diagnosis of radiopharmaceuticals must be suspended for a while. Inconvenience. Therefore, the contaminated air generated by a slight leak from the automatic synthesizer installed in the synthesis chamber is carried to the exhaust purification equipment of the radiation facility by a duct connected to the synthesis chamber, where the granular activated carbon filter, HEPA filter or ULPA Purified by a filter.
一方、18F FDGを合成する際には未反応のフッ化水素(HF)がガス成分に多量に含まれているが、HEPAフィルターやULPAフィルターはガス成分の浄化には対応していない。ガス成分の浄化に対応するためには、一般的には放射線施設の排気浄化設備に粒状活性炭フィルターが設置される。排気浄化設備における粒状活性炭フィルターは、空気中に含まれる微量ガスや湿気を吸着するが、それによって18Fガス及び中間生成物の捕集性能が劣化(ウェザリング)する。また、排気浄化設備は、合成室以外の室内空気も浄化するようにダクトが接続されているため、劣化が激しく、処理風量や粉塵量も多いため、交換する場合にフィルターが大型となりコスト高となる。 On the other hand, when synthesizing 18 F FDG, a large amount of unreacted hydrogen fluoride (HF) is contained in the gas component, but the HEPA filter and ULPA filter do not support purification of the gas component. In order to cope with purification of gas components, a granular activated carbon filter is generally installed in an exhaust purification facility of a radiation facility. The granular activated carbon filter in the exhaust purification equipment adsorbs trace gases and moisture contained in the air, but this deteriorates (weathering) the collection performance of 18 F gas and intermediate products. In addition, because the exhaust purification equipment is connected with ducts so as to purify indoor air other than the synthesis room, the exhaust purification equipment is severely deteriorated and has a large amount of processing air and dust. Become.
かかる問題を克服するために、アルカリ性物質を添着した活性炭素繊維フィルターを合成室の排気口に設置することによって、微量の放射性物質を除去し、排気設備に排気される放射性物質の量を少なくする方法が提案されている(特許文献1参照)。かかる方法は放射性物質の除去には極めて有効であるが、小規模化、クリーン化が進む昨今の合成設備では、十分な排気設備を設置できないのが現状である。 In order to overcome such problems, an activated carbon fiber filter impregnated with an alkaline substance is installed at the exhaust port of the synthesis chamber, thereby removing a small amount of radioactive substance and reducing the amount of radioactive substance exhausted to the exhaust facility. A method has been proposed (see Patent Document 1). Such a method is extremely effective for removing radioactive substances, but the current situation is that sufficient exhaust facilities cannot be installed in recent synthesis facilities that are becoming smaller and cleaner.
本発明は、上記の従来技術の現状に鑑み創案されたものであり、その目的は、小型化、クリーン化された陽電子放射断層診断装置において使用される18F標識化合物合成室から排出される放射性物質を効率的に除去する方法を提供することにある。 The present invention was devised in view of the current state of the prior art described above, and its purpose is to provide radioactive materials discharged from the 18 F-labeled compound synthesis chamber used in a miniaturized and cleaned positron emission tomography diagnostic apparatus. The object is to provide a method for efficiently removing substances.
本発明者らは、かかる目的を達成するために放射性物質の除去方法について鋭意検討した結果、特定のフィルターユニットの構成及び配置を用いて合成室内部の空気を循環することにより、小型化された合成室でも十分な排気設備を設置できることを見い出し、本発明の完成に至った。 As a result of intensive studies on a method for removing a radioactive substance in order to achieve such an object, the present inventors have reduced the size by circulating air inside the synthesis chamber using a specific filter unit configuration and arrangement. It has been found that sufficient exhaust equipment can be installed in the synthesis room, and the present invention has been completed.
即ち、本発明は、以下の(1)〜(3)の構成を有するものである。
(1)陽電子放射断層診断装置において診断薬として用いられる18F標識化合物を合成する際に合成室内部で発生する放射性物質をフィルターユニットで除去する方法において、フィルターユニットが合成室内部に配設され、フィルターユニットが送風ファン、活性炭素繊維フィルター、および面風速0.4m/sにおける0.3〜0.5μmの粒子捕集効率が90〜99%である除塵フィルターを一体的に備え、フィルターユニットの送風ファンを稼動させて合成室内部の空気をフィルターユニットの活性炭素繊維フィルターおよび除塵フィルターの順に通過させて循環することにより放射性物質を除去すること、および活性炭素繊維フィルターの活性炭素繊維が、アルカリ性物質を添着した活性炭素繊維からなることを特徴とする放射性物質の除去方法。
(2)活性炭素繊維フィルターおよび/または除塵フィルターが、フィルターユニットから取り出し交換可能であることを特徴とする(1)に記載の放射性物質の除去方法。
(3)フィルターユニットが、送風ファンの上流側に空気を取り入れるための空隙を有することを特徴とする(1)または(2)に記載の放射性物質の除去方法。
That is, the present invention has the following configurations (1) to ( 3 ).
(1) In a method of removing radioactive substances generated in a synthesis chamber when synthesizing an 18 F-labeled compound used as a diagnostic agent in a positron emission tomography diagnostic apparatus, the filter unit is disposed in the synthesis chamber. The filter unit is integrally provided with a blower fan, an activated carbon fiber filter, and a dust removal filter having a particle collection efficiency of 0.3 to 0.5 μm at a surface wind speed of 0.4 m / s of 90 to 99%. The activated air fiber fan is operated to remove the radioactive material by circulating the air in the synthetic chamber through the activated carbon fiber filter and the dust filter of the filter unit in this order , and the activated carbon fiber of the activated carbon fiber filter is radiation, characterized in that it consists of activated carbon fibers impregnated with an alkaline substance Method of removing the substance.
( 2 ) The method for removing a radioactive substance according to ( 1), wherein the activated carbon fiber filter and / or the dust removal filter can be removed from the filter unit and exchanged.
( 3 ) The method for removing a radioactive substance according to (1) or (2 ), wherein the filter unit has a gap for taking in air upstream of the blower fan.
本発明の方法によれば、フィルターユニットが発塵量の少ない活性炭素繊維フィルターと圧損の少ない比較的高効率な除塵フィルターを使用しているので、フィルターユニットからの発塵量を少量に抑制した上で十分な風量を確保することができる。さらに、本発明の方法によれば、フィルターユニットを合成室内部に取付け、送風ファンによって合成室内部の空気を循環しているので、合成室内部の清浄度を低下させることなく18Fガス及び中間生成物の局所捕集ができ、放射線科全体の排気浄化設備に設置したフィルターユニットによる除去に比べて極めて効率の良い排気処理が可能である。 According to the method of the present invention, the filter unit uses an activated carbon fiber filter with a small amount of dust generation and a relatively high-efficiency dust removal filter with a small pressure loss, so that the amount of dust generated from the filter unit is suppressed to a small amount. Sufficient air volume can be secured above. Furthermore, according to the method of the present invention, attaching the filter unit to the synthesis chamber portion, since the circulating air in the synthesis chamber portion by the blower fan, 18 F gas and an intermediate without reducing the cleanliness of the synthesis chamber portion The product can be collected locally, and it is possible to perform exhaust treatment that is very efficient compared to the removal by the filter unit installed in the exhaust purification equipment of the entire radiology department.
本発明の放射性物質の除去方法を以下に説明するが、本発明はこれに限定されるものではない。 The method for removing a radioactive substance of the present invention will be described below, but the present invention is not limited to this.
図1は、18F標識物質の合成室内に設置するフィルターユニットの概略断面図を示し、図2は、フィルターユニットの外観斜視図を示す。フィルターユニットは、送風ファン1、活性炭素繊維フィルター2、および比較的高効率であるが通気抵抗の少ない除塵フィルター3をこの順序で連続して一体的に備え、これらは金属製の筐体4内に設置されている。活性炭素繊維フィルター2と除塵フィルター3は、フィルターユニット下流側から押さえ枠5を使って固定される。送風ファン1の上流側には、空気を吸入できる空隙6を有しており、送風ファン1が回転すると、空隙6より空気を取り込み、活性炭素繊維フィルター2、除塵フィルター3を通じて放射性物質が除去される。フィルターユニットは、18F標識物質の合成室内の一角に静置され、合成室内部の空気がフィルターユニットを通じて循環することによって合成室内部の放射性物質が除去される。 FIG. 1 shows a schematic cross-sectional view of a filter unit installed in the synthesis chamber of 18 F-labeled substance, and FIG. 2 shows an external perspective view of the filter unit. The filter unit includes a blower fan 1, an activated carbon fiber filter 2, and a dust filter 3 that is relatively highly efficient but has a low airflow resistance in this order, and is integrated in a metal housing 4. Is installed. The activated carbon fiber filter 2 and the dust removal filter 3 are fixed using a pressing frame 5 from the downstream side of the filter unit. On the upstream side of the blower fan 1, there is a gap 6 through which air can be sucked. When the blower fan 1 rotates, the air is taken in from the gap 6 and radioactive substances are removed through the activated carbon fiber filter 2 and the dust removal filter 3. The The filter unit is allowed to stand at one corner of the 18 F-labeled substance synthesis chamber, and the air inside the synthesis chamber circulates through the filter unit to remove the radioactive substance inside the synthesis chamber.
18F標識物質の合成室内部は、粉塵の清浄度が高く保持されているためフィルターユニットからの発塵は極めて制限されていることが必要である。本発明では、比較的発塵量が少ない活性炭素繊維フィルター2を採用し、その下流側に比較的高効率であるが通気抵抗の少ない除塵フィルター3を設置することによって、活性炭素繊維フィルター2からの発塵を防止しながら通気抵抗を抑制していることが特徴である。除塵フィルター3は、一般的なクリーンルームなどでのFFU(ファンフィルターユニット)において使用されるHEPAフィルターやULPAフィルターは使用されない。HEPAフィルターやULPAフィルターは、その除塵効率が極めて高いもののフィルターの通気抵抗が高いため、通常の送風ファンを用いると風量が低下して効率的に好ましくない。HEPAフィルターやULPAフィルターは、発塵量の多い粒状活性炭フィルターと組み合わせて用いられるが、やはり風量が低下する問題がある。このため、より発塵の少ない活性炭素繊維フィルターと、圧力損失が低く除塵効率が比較的高い除塵フィルターを組み合わせて用いることが効率的である。 Since the cleanliness of dust is kept high in the 18 F-labeled substance synthesis chamber, dust generation from the filter unit must be extremely limited. In the present invention, the activated carbon fiber filter 2 having a relatively small amount of dust generation is employed, and the dust removing filter 3 having a relatively high efficiency but a low airflow resistance is installed on the downstream side of the activated carbon fiber filter 2, thereby It is characterized by suppressing airflow resistance while preventing dust generation. As the dust removal filter 3, a HEPA filter or a ULPA filter used in an FFU (fan filter unit) in a general clean room or the like is not used. Although the HEPA filter and the ULPA filter have extremely high dust removal efficiency, the airflow resistance of the filter is high. Therefore, when a normal blower fan is used, the air volume is lowered, which is not preferable. HEPA filters and ULPA filters are used in combination with granular activated carbon filters that generate a large amount of dust, but there is still a problem that the air volume is reduced. For this reason, it is efficient to use a combination of an activated carbon fiber filter with less dust generation and a dust removal filter with low pressure loss and relatively high dust removal efficiency.
本発明に用いられる活性炭素繊維フィルター2は、放射性物質の捕集のためのものであり、粒状活性炭フィルターと比べて発塵量が極めて少ないという特徴を有する。活性炭素繊維は、有機系物質を吸着除去する性質があるが、少なくとも1種類以上のアルカリ物質が添着されることにより酸性を呈した放射性物質も除去することができる。また、活性炭素繊維は、シート状に加工すると、公知の粒状炭充填フィルターに見られる運転中の微振動による活性炭の発塵が殆どない。図3は、本発明に用いられる活性炭素繊維フィルターを示す。活性炭素繊維7は、シート化されてジグザグ状に折られた後、山と山の間に波型のセパレーター8を挿入して空気の流通路を確保し、枠体9で固定化して活性炭素繊維フィルター2になる。活性炭素繊維フィルター2は、フィルターユニットの筐体4の内部の送風ファン1の下流側に設置される。活性炭素繊維に添着されるアルカリ物質は、アルカリ、アルカリ土類金属の水酸化物や炭酸塩、またはアミン類が好適に使用される。 The activated carbon fiber filter 2 used in the present invention is for collecting radioactive substances, and has a feature that the amount of dust generation is extremely small compared to a granular activated carbon filter. Activated carbon fiber has the property of adsorbing and removing organic substances, but it can also remove acidic radioactive substances by adding at least one alkaline substance. Further, when the activated carbon fiber is processed into a sheet shape, the activated carbon fiber hardly generates dust from the activated carbon due to the slight vibration during operation, which is found in a known granular carbon-filled filter. FIG. 3 shows an activated carbon fiber filter used in the present invention. After the activated carbon fiber 7 is formed into a sheet and folded in a zigzag shape, a corrugated separator 8 is inserted between the peaks to secure an air flow path, and the activated carbon fiber 7 is fixed by the frame body 9 to be activated carbon. It becomes the fiber filter 2. The activated carbon fiber filter 2 is installed on the downstream side of the blower fan 1 inside the housing 4 of the filter unit. As the alkaline substance to be attached to the activated carbon fiber, alkali, alkaline earth metal hydroxide or carbonate, or amines are preferably used.
本発明に用いられる除塵フィルター3は、主に活性炭素繊維フィルター2から発生しうる微粉塵を除去するために設けられるものであり、風量を確保するために低い圧力損失のものを用いる。具体的には、除塵フィルター3は、面風速0.4m/sにおける0.3〜0.5μmの粒子捕集効率が90%以上、さらには92%以上、そして99%以下、さらには98%以下を有することが好ましい。なお、ここでいう面風速とは、フィルターで設定されている風量をフィルターの開口部分の寸法で除した値を指す。フィルターの圧力損失と捕集効率は一定の面風速においては補完関係に有り、例えば捕集効率が高すぎると風量を確保できず、一方低すぎると十分な除塵機能を果たせなくなる。一般的に公知のガラス繊維で構成されたHEPAフィルターやULPAフィルター用のろ材は、非常に高効率であるが通気抵抗が高く好ましくない。また、除去対象物質の中にはガラスを腐食するフッ化水素が存在するため好ましくない。本発明では、放射性物質の除去のために発塵量の少ない活性炭素繊維フィルターが用いられているため、下流側にHEPAフィルターやULPAフィルターほどの高効率なフィルターを用いる必要がなく、風量の確保(低通気抵抗)を優先することができる。除塵フィルター3は、上記特性を満たす限り特に限定されないが、高分子系のろ材が好ましく、特に薬品耐性の強いポリオレフィン系を公知の方法で荷電した静電ろ材を公知の方法でフィルター化したものが好ましい。除塵フィルター3は、活性炭素繊維フィルターの下流側に設置され、この場合、活性炭素繊維フィルターとの密着性を良くすると微粉塵のリークを効果的に防止することができる。活性炭素繊維フィルター2と除塵フィルター3の筐体4は、アルミニウムやステンレスなどの耐腐食性金属で構成され、両者の間にはクロロプレンで構成されたパッキンを挟んだ状態で固定化されることが好ましい。 The dust removal filter 3 used in the present invention is provided mainly for removing fine dust that can be generated from the activated carbon fiber filter 2, and uses a filter with a low pressure loss in order to secure the air volume. Specifically, the dust removal filter 3 has a particle collection efficiency of 0.3 to 0.5 μm at a surface wind speed of 0.4 m / s of 90% or more, further 92% or more, and 99% or less, and further 98%. Preferably it has: The surface wind speed here refers to a value obtained by dividing the air volume set by the filter by the size of the opening of the filter. The filter pressure loss and the collection efficiency are in a complementary relationship at a constant surface wind speed. For example, if the collection efficiency is too high, the air volume cannot be secured, while if it is too low, a sufficient dust removal function cannot be performed. In general, a filter medium for a HEPA filter or a ULPA filter composed of a known glass fiber has a very high efficiency but is not preferable because of high ventilation resistance. Moreover, since the hydrogen fluoride which corrodes glass exists in the substance to be removed, it is not preferable. In the present invention, an activated carbon fiber filter with a small amount of dust generation is used to remove radioactive substances, so that it is not necessary to use a filter as highly efficient as a HEPA filter or ULPA filter on the downstream side, ensuring air volume. (Low ventilation resistance) can be prioritized. The dust removal filter 3 is not particularly limited as long as the above characteristics are satisfied, but a polymer filter medium is preferable, and a filter medium obtained by filtering an electrostatic filter medium charged with a known chemical-resistant polyolefin system by a known method. preferable. The dust removal filter 3 is installed on the downstream side of the activated carbon fiber filter. In this case, if the adhesion with the activated carbon fiber filter is improved, the leakage of fine dust can be effectively prevented. The housing 4 of the activated carbon fiber filter 2 and the dust filter 3 is made of a corrosion-resistant metal such as aluminum or stainless steel, and may be fixed with a packing made of chloroprene sandwiched between them. preferable.
筐体4で固定された活性炭素繊維フィルター2や除塵フィルター3は、フィルターユニットから取り出し交換可能なように最下流から押さえ枠5で押すように固定化され、フィルターユニットの筐体4にねじ止めされる。 The activated carbon fiber filter 2 and the dust removal filter 3 fixed in the casing 4 are fixed so as to be removed from the filter unit and exchanged with the pressing frame 5 from the most downstream side, and screwed to the casing 4 of the filter unit. Is done.
以下に実施例によって本発明の方法の効果を示すが、以下の実施例は本発明を制限するものではなく、本発明の趣旨を逸脱しない範囲で変更実施することができる。 The effects of the method of the present invention will be described below by way of examples. However, the following examples are not intended to limit the present invention and can be modified without departing from the spirit of the present invention.
(実施例1)
(筐体)
厚み1.5mmのSUS304で外寸185mm角、奥行220mmの筐体を用意し、一方の側にフレーム付ACファン160mm角(定格風量7m3/min)をファンの風が筐体内部に流通するように取り付けた。ファンの上流側に長さ50mm、幅20mmのアルミニウム製L字棒を4隅に取り付け、設置した際の空気流入口(空隙)を確保した。
Example 1
(Casing)
A case of SUS304 with a thickness of 1.5 mm and an outer size of 185 mm square and a depth of 220 mm is prepared, and a 160 mm square AC fan with a frame (rated air volume 7 m 3 / min) is distributed on the inside of the fan. It was attached as follows. An aluminum L-shaped bar having a length of 50 mm and a width of 20 mm was attached to the four corners on the upstream side of the fan, and an air inlet (gap) was secured when installed.
(活性炭素繊維フィルター)
1,4−ジアザビシクロ−(2,2,2)オクタン(DABCO)を14重量%添着し、目付230g/m2、厚み2.8mm、比表面積1500m2/g、繊維径12μmの繊維状活性炭からなる不織布シート2枚を目付30g/m2のポリプロピレン製スパンレース不織布で上下から挟み、ニードルパンチしてシート化した。山高130mm、山数7でジグザグに折り、山と山の間に波型に加工されたポリエチレンコート紙をはさんで幅176mmにスリットし、ウレタン系樹脂を内側に塗布したアルミ枠(180mm角、奥行き150mm)にセットして活性炭素繊維フィルターを作成した。
(Activated carbon fiber filter)
From fibrous activated carbon impregnated with 14% by weight of 1,4-diazabicyclo- (2,2,2) octane (DABCO), having a basis weight of 230 g / m 2 , a thickness of 2.8 mm, a specific surface area of 1500 m 2 / g, and a fiber diameter of 12 μm Two nonwoven fabric sheets to be formed were sandwiched from above and below with a polypropylene spunlace nonwoven fabric having a basis weight of 30 g / m 2 and formed into a sheet by needle punching. Aluminum frame (180 mm square, 180 mm square, with a height of 130 mm, folded into zigzags at 7 peaks, slit into a width of 176 mm with a corrugated polyethylene coated paper between the peaks, and urethane resin applied inside An activated carbon fiber filter was prepared by setting the depth to 150 mm.
(除塵フィルター)
目付145g/m2、厚み0.5mm、風速10cm/sにおける圧力損失60Pa、風速10cm/sにおける0.3〜0.5μmの粒子捕集効率が93%のポリエステル/ポリプロピレン系不織布で構成された静電ろ材を用意し、公知の方法で山高45mm、山ピッチ5.0mmのアルミ枠(180mm角、奥行き50mm)を用いて除塵フィルターを作成した。作成されたフィルターの面風速0.4m/sにおける圧力損失は12Pa、面風速0.4m/sにおける0.3〜0.5μmの粒子捕集効率は98.2%であった。
(Dust removal filter)
It is composed of a polyester / polypropylene nonwoven fabric having a basis weight of 145 g / m 2 , a thickness of 0.5 mm, a pressure loss of 60 Pa at a wind speed of 10 cm / s, and a particle collection efficiency of 0.3 to 0.5 μm at a wind speed of 10 cm / s of 93%. An electrostatic filter medium was prepared, and a dust removal filter was prepared by a known method using an aluminum frame (180 mm square, 50 mm depth) having a mountain height of 45 mm and a mountain pitch of 5.0 mm. The produced filter had a pressure loss of 12 Pa at a surface wind speed of 0.4 m / s, and a particle collection efficiency of 0.3 to 0.5 μm at a surface wind speed of 0.4 m / s was 98.2%.
(フィルターユニット)
筐体に固定されたフレーム付ACファンの下流側に両側の枠体にクロロプレン発泡パッキン(10mm幅×5mm厚)を貼付した活性炭素繊維フィルターを設置し、筐体内に設置した。さらに、除塵フィルターをその下流側に設置して180角、奥行き10mm、厚み1.5mmのステンレス枠を最下流から筐体に挿入してねじ止めし、フィルターを筐体に固定し、フィルターユニットを作成した。
(Filter unit)
An activated carbon fiber filter in which chloroprene foam packing (10 mm width × 5 mm thickness) was attached to the frames on both sides was installed on the downstream side of the frame-equipped AC fan fixed to the housing, and installed in the housing. Furthermore, a dust removal filter is installed on the downstream side, a 180 square, 10 mm deep, 1.5 mm thick stainless steel frame is inserted into the housing from the most downstream side and screwed, the filter is fixed to the housing, and the filter unit is mounted. Created.
(下流側の発塵粒子数とフィルターユニットの風速の測定)
上流側から粉塵を含んでいない清浄空気中にて上記のフィルターユニットのファンを稼動させ、そのときに下流側で発生した0.3μm以上の粉塵数をパーティクルカウンター(リオン株式会社製KC−01E)で0.3L採取して測定した。フィルターユニットの風速は、ユニット下流側に250mmのフードを取り付けてプロペラ式風速計で測定した。このときの風速は1.7m/sであり、0.3μm以上の粉塵数は確認されなかった。
(Measurement of the number of dust particles on the downstream side and the wind speed of the filter unit)
The fan of the above filter unit is operated in clean air containing no dust from the upstream side, and the particle count (KC-01E manufactured by Lion Co., Ltd.) 0.3 L was collected and measured. The wind speed of the filter unit was measured with a propeller-type anemometer with a 250 mm hood attached downstream of the unit. The wind speed at this time was 1.7 m / s, and the number of dusts of 0.3 μm or more was not confirmed.
(実施例2)
目付115g/m2、厚み0.9mm、風速10cm/sにおける圧力損失40Pa、風速10cm/sにおける0.3〜0.5μmの粒子捕集効率が78%のポリエステル/ポリプロピレン系不織布で構成された静電ろ材を用意し、公知の方法で山高45mm、山ピッチ5.0mmのアルミ枠(180mm角、奥行き50mm)を用いて除塵フィルターを作成した。作成されたフィルターの面風速0.4m/sにおける圧力損失は22Pa、面風速0.4m/sにおける0.3〜0.5μmの粒子捕集効率は92.2%であった。除塵フィルターの作成以外は、実施例1と同様にフィルターユニットを作成し、評価した。このときの風速は1.8m/sであり、0.3μm以上の粉塵数は確認されなかった。
(Example 2)
It was composed of a polyester / polypropylene nonwoven fabric having a basis weight of 115 g / m 2 , a thickness of 0.9 mm, a pressure loss of 40 Pa at a wind speed of 10 cm / s, and a particle collection efficiency of 0.3 to 0.5 μm at a wind speed of 10 cm / s of 78%. An electrostatic filter medium was prepared, and a dust removal filter was prepared by a known method using an aluminum frame (180 mm square, 50 mm depth) having a mountain height of 45 mm and a mountain pitch of 5.0 mm. The produced filter had a pressure loss of 22 Pa at a surface wind speed of 0.4 m / s, and a particle collection efficiency of 0.3 to 0.5 μm at a surface wind speed of 0.4 m / s was 92.2%. A filter unit was prepared and evaluated in the same manner as in Example 1 except for the preparation of the dust removal filter. The wind speed at this time was 1.8 m / s, and the number of dusts of 0.3 μm or more was not confirmed.
(比較例1)
除塵フィルターをフッ素膜系ULPAフィルター(180mm角、奥行き50mm、面風速0.4m/sにおける圧力損失150Pa、面風速0.4m/sにおける0.3〜0.5μmの粒子捕集効率が99.9995%)に交換した以外は、上記の実施例と同様にしてフィルターユニットを作成し、評価した。0.3μm以上の粉塵数は確認されなかったものの、風速は0.4m/sであった。
(Comparative Example 1)
The dust filter is a fluorine membrane ULPA filter (180 mm square, depth 50 mm, pressure loss 150 Pa at a surface wind speed of 0.4 m / s, particle collection efficiency of 0.3 to 0.5 μm at a surface wind speed of 0.4 m / s is 99. A filter unit was prepared and evaluated in the same manner as in the above example, except that it was changed to 9995%). Although the number of dusts of 0.3 μm or more was not confirmed, the wind speed was 0.4 m / s.
(比較例2)
除塵フィルターをフッ素膜系HEPAフィルター(180mm角、奥行き50mm、面風速0.4m/sにおける圧力損失70Pa、面風速0.4m/sにおける0.3〜0.5μmの粒子捕集効率が99.997%)に交換した以外は、上記の実施例と同様にしてフィルターユニットを作成し、評価した。0.3μm以上の粉塵数は確認されなかったものの、風速は0.6m/sであった。
(Comparative Example 2)
The dust removal filter is a fluorine membrane HEPA filter (180 mm square, depth 50 mm, pressure loss 70 Pa at a surface wind speed of 0.4 m / s, and particle collection efficiency of 0.3 to 0.5 μm at a surface wind speed of 0.4 m / s is 99.99 μm. A filter unit was prepared and evaluated in the same manner as in the above example except that it was changed to 997%. Although the number of dusts of 0.3 μm or more was not confirmed, the wind speed was 0.6 m / s.
(比較例3)
目付97g/m2、厚み1.0mm、風速10m/sにおける圧力損失40Pa、風速10m/sにおける0.3〜0.5μmの粒子捕集効率が63%のポリプロピレン系不織布で構成された静電ろ材を用意し、公知の方法で山高45mm、山ピッチ5.0mmのアルミ枠(180mm角、奥行き50mm)を用いて除塵フィルターを作成した。作成されたフィルターの面風速0.4m/sにおける圧力損失は20Pa、面風速0.4m/sにおける0.3〜0.5μmの粒子捕集効率は83.1%であった。除塵フィルターの作成以外は、実施例1と同様にフィルターユニットを作成し、評価した。このときの風速は1.8m/sであり、0.3μm以上の粉塵数が5個確認された。
(Comparative Example 3)
An electrostatic capacity composed of a polypropylene nonwoven fabric having a basis weight of 97 g / m 2 , a thickness of 1.0 mm, a pressure loss of 40 Pa at a wind speed of 10 m / s, and a particle collection efficiency of 0.3 to 0.5 μm at a wind speed of 10 m / s of 63%. A filter medium was prepared, and a dust removal filter was prepared by a known method using an aluminum frame (180 mm square, 50 mm depth) having a mountain height of 45 mm and a mountain pitch of 5.0 mm. The produced filter had a pressure loss of 20 Pa at a surface wind speed of 0.4 m / s and a particle collection efficiency of 0.3 to 0.5 μm at a surface wind speed of 0.4 m / s of 83.1%. A filter unit was prepared and evaluated in the same manner as in Example 1 except for the preparation of the dust removal filter. The wind speed at this time was 1.8 m / s, and five dust counts of 0.3 μm or more were confirmed.
本発明の方法によれば、小型化、クリーン化された陽電子放射断層診断装置において使用される18F標識化合物合成室から排出される放射性物質を効率的に除去することができる。 According to the method of the present invention, the radioactive substance discharged from the 18 F-labeled compound synthesis chamber used in the miniaturized and cleaned positron emission tomography diagnostic apparatus can be efficiently removed.
1 送風ファン
2 活性炭素繊維フィルター
3 除塵フィルター
4 筐体
5 押さえ枠
6 空隙
7 活性炭素繊維ろ材
8 セパレーター
9 外枠
DESCRIPTION OF SYMBOLS 1 Blower fan 2 Activated carbon fiber filter 3 Dust removal filter 4 Case 5 Holding frame 6 Cavity 7 Activated carbon fiber filter material 8 Separator 9 Outer frame
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