JPS5930653B2 - Microwave heating denitrification equipment - Google Patents
Microwave heating denitrification equipmentInfo
- Publication number
- JPS5930653B2 JPS5930653B2 JP56071686A JP7168681A JPS5930653B2 JP S5930653 B2 JPS5930653 B2 JP S5930653B2 JP 56071686 A JP56071686 A JP 56071686A JP 7168681 A JP7168681 A JP 7168681A JP S5930653 B2 JPS5930653 B2 JP S5930653B2
- Authority
- JP
- Japan
- Prior art keywords
- heated
- container
- microwave
- microwave heating
- denitrification
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/12—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electromagnetic waves
- B01J19/122—Incoherent waves
- B01J19/126—Microwaves
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J2219/12—Processes employing electromagnetic waves
- B01J2219/1203—Incoherent waves
- B01J2219/1206—Microwaves
- B01J2219/1209—Features relating to the reactor or vessel
- B01J2219/1212—Arrangements of the reactor or the reactors
- B01J2219/1215—Single reactor
Landscapes
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Constitution Of High-Frequency Heating (AREA)
- Electric Ovens (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Description
【発明の詳細な説明】
本発明は、たとえば、硝酸ウラニル溶液もしくは硝酸プ
ルトニウム溶液またはこれらの混合溶液を加熱して核燃
料製造用の酸化ウランもしくは酸化プルトニウムまたは
これらの混合酸化物を得るマイクロ波加熱脱硝装置に係
り、特に被加熱物収容容器を窒化珪素セラミックスまた
はマイカセラミックスにて形成したマイクロ波加熱脱硝
装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a microwave heating denitrification method for producing uranium oxide, plutonium oxide, or a mixed oxide thereof for nuclear fuel production by heating a uranyl nitrate solution, a plutonium nitrate solution, or a mixed solution thereof, for example. The present invention relates to an apparatus, and particularly to a microwave heating denitrification apparatus in which a heated object storage container is formed of silicon nitride ceramics or mica ceramics.
硝酸ウラニル溶液もしくは硝酸プルトニウム溶液または
これらの混合溶液にマイクロ波を照射して加熱すると、
第1図中に実線で示すように、まず約120℃まで昇温
したA。When uranyl nitrate solution, plutonium nitrate solution, or a mixed solution of these is heated by irradiation with microwaves,
As shown by the solid line in FIG. 1, A was first heated to about 120°C.
点で沸騰が始まり、溶液は濃縮されて硝酸塩を析出する
。次いで硝酸塩が乾燥するB。点あたりから再び昇温し
、約300℃に達したCo点あたりから脱硝反応が進行
し、酸化ウランもしくは酸化プルトニウムまたはこれら
の混合酸化物となり、このような酸化物は核燃料の製造
に使用される。以上のような用途に使用されるマイクロ
波加熱脱硝装置としては、従来ではステンレス鋼よりな
る収容容器に加熱すべき溶液を入れ、マイクロ波を照射
するようにしていた。At this point boiling begins and the solution concentrates to precipitate the nitrates. B. The nitrate is then dried. The temperature rises again from around this point, and the denitrification reaction progresses from around the Co point when it reaches approximately 300°C, forming uranium oxide, plutonium oxide, or a mixed oxide of these.Such oxides are used in the production of nuclear fuel. . Conventionally, in a microwave heating denitrification apparatus used for the above-mentioned applications, a solution to be heated is placed in a container made of stainless steel, and the solution is irradiated with microwaves.
ところが、このような構成ではマイクロ波が収容容器で
反射されるため、容器内の溶液には容器の上部開口を通
してのみマイクロ波が照射されることになり、加熱効率
が悪いため2OKW以上もの大出力を要し、かつ長時間
を要していた。However, in such a configuration, the microwave is reflected by the container, so the solution in the container is irradiated with microwaves only through the upper opening of the container, resulting in poor heating efficiency and a high output of more than 2 OKW. and took a long time.
また溶液全体が均一に加熱されず、未脱硝部が残る問題
もあつた。そこで、収容容器の材質をマイクロ波が透過
するようなものにすることが考えられるわけであるが、
マイクロ波を透過させる材質として一般に知られている
ガラス、アルミナセラミックスなどは強度が低いので、
移送時に破損するおそれがある。There was also the problem that the entire solution was not heated uniformly, leaving undenitrated portions. Therefore, it may be possible to use a material for the container that allows microwaves to pass through.
Glass and alumina ceramics, which are generally known as materials that transmit microwaves, have low strength, so
There is a risk of damage during transportation.
また、脱硝には一般の電子レンジとは比較にならない程
大きなマイクロ出力を必要とし、特に被加熱物が液相か
ら固相へ変化する際には大出力を要するため、収容容器
には脱硝反応の終了点付近できわめて大きな熱衝撃が作
用することになるが、ガラス、アルミナセラミックスな
どは熱衝撃にも弱く、マイクロ波加熱脱硝装置の被加熱
物収容容器として使用するには不向きであつた。本発明
はこのような事情にもとづいてなされたもので、その目
的は、被加熱物収容容器を窒化珪素セラミツクスまたは
マイカセラミツクスにて形成することにより、被加熱物
収容容器が破損しにくく、また被加熱物を比較的小出力
で速やかに、かつ均一に加熱できるマイクロ波加熱脱硝
装置を提供することにある。In addition, denitrification requires a micro-output that is incomparably larger than that of a general microwave oven, and especially when the object to be heated changes from a liquid phase to a solid phase, a large output is required. A very large thermal shock will be applied near the end point of the process, but glass, alumina ceramics, etc. are susceptible to thermal shock and are unsuitable for use as containers for heated objects in microwave heating denitrification equipment. The present invention has been made based on the above-mentioned circumstances, and an object thereof is to make the heated object storage container less likely to be damaged by forming the heated object storage container from silicon nitride ceramics or mica ceramics. It is an object of the present invention to provide a microwave heating denitrification device that can quickly and uniformly heat a heated object with a relatively low output.
以下、本発明の構成を第2図に示す実施例にもとづいて
説明する。The configuration of the present invention will be explained below based on the embodiment shown in FIG.
図中1はたとえばステンレス鋼などの金属板よりなるマ
イクロ波オーブンで、このオーブン1は底部中央に開口
部1Aを有し、この開口部1Aは昇降台2でマイクロ波
を通さない程度に閉塞されている。In the figure, 1 is a microwave oven made of a metal plate such as stainless steel, and this oven 1 has an opening 1A at the center of the bottom, and this opening 1A is closed by an elevator platform 2 to an extent that microwaves cannot pass through. ing.
昇降台2は5駆動部2Aにより昇降駆動され、図に実線
で示す位置で前記開口部1Aを閉塞してマイクロ波オー
ブン1内の雰囲気を外部と遮断し、オーブン1の内部空
間をマイクロ波照射場にする。前記昇降台2には被加熱
物収容容器3が載置され、この容器3の内部には、硝酸
ウラニル溶液、硝酸プルトニウム溶液またはこれらの混
合溶液のような、加熱、脱硝すべき被加熱物4が収容さ
れる。前記被加熱物収容容器3は、窒化珪素セラミツク
スまたはマイカセラミツクスによつて形成されている。The lifting platform 2 is driven up and down by a 5-driving unit 2A, and the opening 1A is closed at the position shown by the solid line in the figure to isolate the atmosphere inside the microwave oven 1 from the outside, and the internal space of the oven 1 is irradiated with microwaves. Make it a place. A container 3 for storing objects to be heated is placed on the lifting platform 2, and inside this container 3 there is a heated object 4 to be heated and denitrified, such as a uranyl nitrate solution, a plutonium nitrate solution, or a mixed solution thereof. is accommodated. The heated object storage container 3 is made of silicon nitride ceramics or mica ceramics.
窒化珪素セラミツクスおよびマイカセラミツクスの成分
および耐熱衝撃性は次の通りである。ちなみに、ソーダ
ガラスの耐熱衝撃性(水中に落しても割れない最高温度
)は94℃程度であり、アルミナセラミツクスは40℃
程度であるから、窒化珪素セラミツクス、マイカセラミ
ツクスのいずれも耐熱衝撃性がきわめて優れていること
は明らかである。The components and thermal shock resistance of silicon nitride ceramics and mica ceramics are as follows. By the way, the thermal shock resistance of soda glass (the maximum temperature at which it will not break even if dropped into water) is around 94℃, and that of alumina ceramics is 40℃.
It is clear that both silicon nitride ceramics and mica ceramics have extremely excellent thermal shock resistance.
また、前記マイクロ波オーブン1の土部にはマイクロ波
発振器5が導波管6を介して接続され、さらに光検出器
7および排気管8が接続されている。Further, a microwave oscillator 5 is connected to the soil portion of the microwave oven 1 via a waveguide 6, and a photodetector 7 and an exhaust pipe 8 are further connected.
次に、以上の如く構成されたマイクロ波加熱装置の作用
を説明する。Next, the operation of the microwave heating device configured as above will be explained.
まず被加熱物収容容器3に、硝酸ウラニル溶液、硝酸プ
ルトニウム溶液またはこれらの混合溶液などの被加熱物
4を入れ、また駆動部2Aにより昇降台2を第2図に仮
想線で示す位置まで下降させ、この昇降台2に被加熱物
4を入れた収容容器3を載置する。First, a heated object 4 such as a uranyl nitrate solution, a plutonium nitrate solution, or a mixed solution thereof is put into the heated object storage container 3, and the lifting platform 2 is lowered by the drive unit 2A to the position shown by the imaginary line in FIG. Then, the storage container 3 containing the object to be heated 4 is placed on the lifting table 2.
次に1駆動部2Aにより昇降台2を第2図中実線で示す
位置まで上昇させると、マイクロ波オーブン1の開口部
1Aがこの昇降台2によりマイクロ波を通さない程度に
閉塞され、オーブン1の内部空間がマイクロ波照射場と
なる。Next, when the lifting table 2 is raised by the driving unit 2A to the position shown by the solid line in FIG. The internal space becomes the microwave irradiation field.
次にマイクロ波発振器5を作動させると、この発振器5
より発振したマイクロ波は導波管6を通してオーブン1
内へ照射され、収容容器3内の被加熱物4に吸収される
。Next, when the microwave oscillator 5 is activated, this oscillator 5
The more oscillated microwaves pass through the waveguide 6 to the oven 1.
The light is irradiated inward and absorbed by the object to be heated 4 inside the container 3.
そこで被加熱物4はマイクロ波照射によつて加熱され、
第1図中に破線で示す如くまず約120℃まで昇温した
A点で沸騰が始まり、溶液は濃縮されて硝酸塩を析出す
る。次いでB点あたりで硝酸塩の乾燥が終了すると再び
昇温し、約300℃に達したC点あたりから脱硝反応が
進行して酸化ウラン、酸化プルトニウムまたはこれらの
混合酸化物となる。このとき、オーブン1内へ照射され
たマイクロ波は、収容容器3の上部開口を通して直接被
加熱物4に吸収されることは勿論であるが、収容容器3
がマイクロ波を透過させる窒化珪素セラミツクスまたは
マイカセラミツクスにて形成されているので、この収容
容器3を透過して被加熱物4に吸収される。したがつて
、第1図中の実線と破線の比較から明らかなように、被
加熱物4は全域に亘つて加熱、蒸発、脱硝が最高10.
4KW程度の小出力で速やかに行なわれ、短時間のうち
に均一な酸化物となる。なお、脱硝反応終了点付近では
マイクロ波の局部集中が生じ、被加熱物4および収容皿
3の温度が局部的に急上昇することがあるが、収容容器
3を形成している窒化珪素セラミツクスまたはマイカセ
ラミツクスはいずれも耐熱衝撃温度がきわめて高いので
、収容容器3は脱硝反応終了点付近で生ずる熱衝撃にも
十分耐えることができる。また脱硝工程中に発生したガ
スは排気管8を通してオーブン1外へ排出される。そし
て脱硝反応が終了すると、被加熱物4は局部的な温度上
昇によつて発光する。Thereupon, the object to be heated 4 is heated by microwave irradiation,
As shown by the broken line in FIG. 1, boiling begins at point A, where the temperature rises to about 120° C., and the solution is concentrated to precipitate nitrate. Next, when the drying of the nitrate is completed around point B, the temperature is raised again, and from around point C, when the temperature reaches about 300° C., the denitrification reaction proceeds to form uranium oxide, plutonium oxide, or a mixed oxide thereof. At this time, the microwave irradiated into the oven 1 is of course directly absorbed by the object to be heated 4 through the upper opening of the storage container 3.
Since the microwave is made of silicon nitride ceramics or mica ceramics that transmit microwaves, the microwaves are transmitted through the container 3 and absorbed by the object to be heated 4 . Therefore, as is clear from the comparison between the solid line and the broken line in FIG. 1, heating, evaporation, and denitrification of the heated object 4 over the entire area reach a maximum of 10.
The process is carried out quickly with a small output of about 4KW, and a uniform oxide is formed in a short time. Note that near the end point of the denitrification reaction, microwaves may be locally concentrated, and the temperature of the object to be heated 4 and the container dish 3 may locally rise sharply. Since all ceramics have an extremely high thermal shock resistance temperature, the container 3 can sufficiently withstand the thermal shock that occurs near the end point of the denitrification reaction. Further, gas generated during the denitration process is exhausted to the outside of the oven 1 through the exhaust pipe 8. When the denitrification reaction is completed, the object to be heated 4 emits light due to the local temperature rise.
そこで、その光は光量検出器7にて検出され、検出器7
の検出出力により前記マイクロ波発振器5の作動を停止
させる。マイクロ波発振器5の作動停止後、駆動部2A
により昇降台2を再び図中仮想線位置まで下降させるこ
とにより、脱硝された酸化物(被加熱物4)の入つた収
容容器3を外部へ取出すことができる。Therefore, the light is detected by the light amount detector 7, and the detector 7
The operation of the microwave oscillator 5 is stopped by the detected output. After the microwave oscillator 5 stops operating, the drive section 2A
By lowering the lifting platform 2 again to the position shown by the imaginary line in the figure, the container 3 containing the denitrified oxide (material to be heated 4) can be taken out to the outside.
以上の実施例では、マイクロ波オーブン1の底部中央に
開口部1Aを設け、この開口部1Aを通して被加熱物収
容容器3を出し入れする構成にしたが、本発明は必ずし
もこのような構成に限定されるものではない。たとえば
マイクロ波オーブン内を通過するベルトコンベアを設け
、このコンベア上に多数の被加熱物収容容器を載置して
コンベアを作動させ、各収容容器内の被加熱物を連続的
′.″:7*畔咄).1*≦j、;二器を出し入れする
ようにしてもよい。In the above embodiment, the opening 1A is provided at the center of the bottom of the microwave oven 1, and the object to be heated container 3 is taken in and taken out through the opening 1A, but the present invention is not necessarily limited to such a configuration. It's not something you can do. For example, a belt conveyor that passes through a microwave oven is provided, a large number of containers for storing objects to be heated are placed on this conveyor, the conveyor is operated, and the objects to be heated in each container are continuously heated. ″:7*畔咄).1*≦j,; You may put in and take out two vessels.
以上、実施例にもとづいて説明したように、本発明に係
るマイクロ波加熱脱硝装置は、窒化珪素セラミツクスま
たはマイカセラミツクスよりなる被加熱物収容容器と、
この収容容器に収容された被加熱物にマイクロ波を照射
してその被加熱物を加熱するマイクロ波発振器とを備え
て構成されている。As described above based on the embodiments, the microwave heating denitrification apparatus according to the present invention includes a heated object storage container made of silicon nitride ceramics or mica ceramics,
It is configured to include a microwave oscillator that heats the object to be heated by irradiating the object to be heated housed in the container with microwaves.
したがつて、被加熱物収容容器は強度上優れているので
、この収容容器が移送時等において破損するおそれはな
く、またマイクロ波が収容容器を透過するので、被加熱
物は小出力のマイクロ波によつて速やかにかつ均一に加
熱され、硝酸ウラニル溶液、硝酸プルトニウム溶液など
の脱硝を容易に行なうことができる。Therefore, since the container for storing objects to be heated has excellent strength, there is no risk of the container being damaged during transportation, and since microwaves pass through the container, objects to be heated can be heated using a low-power microwave. It is heated quickly and uniformly by the waves, making it easy to denitrify uranyl nitrate solutions, plutonium nitrate solutions, and the like.
第1図は硝酸ウラニル溶液もしくは硝酸プルトニウム溶
液またはこれらの混合溶液をマイクロ波照射により加熱
した場合のマイクロ波照射時間と加熱温度との関係を示
すグラフ図、第2図は本発明の一実施例を示す縦断面図
である。
1・・・・・・マイクロ波オーブン、2・・・・・・昇
降台、3・・・・・・被加熱物収容容器、4・・・・・
・被加熱物、5・・・・・・マイクロ波発振器。Figure 1 is a graph showing the relationship between microwave irradiation time and heating temperature when a uranyl nitrate solution, a plutonium nitrate solution, or a mixed solution thereof is heated by microwave irradiation, and Figure 2 is an example of the present invention. FIG. 1...Microwave oven, 2...Elevating platform, 3...Container for heated object, 4...
・Object to be heated, 5...Microwave oscillator.
Claims (1)
りなる被加熱物収容容器と、この収容容器に収容された
被加熱物にマイクロ波を照射してその被加熱物を加熱す
るマイクロ波発振器とを具備したことを特徴とするマイ
クロ波加熱脱硝装置。 2 前記被加熱物収容容器をオーブン内に配置した特許
請求の範囲第1項記載のマイクロ波加熱脱硝装置。 3 前記被加熱物収容容器をオーブン内に昇降自在に配
置した特許請求の範囲第2項記載のマイクロ波加熱脱硝
装置。[Claims] 1. A container for storing objects to be heated made of silicon nitride ceramics or mica ceramics, and a microwave oscillator that heats the objects by irradiating microwaves onto the objects stored in the container. A microwave heating denitrification device characterized by comprising: 2. The microwave heating denitrification apparatus according to claim 1, wherein the object-to-be-heated container is placed in an oven. 3. The microwave heating denitrification apparatus according to claim 2, wherein the object-to-be-heated container is arranged in an oven such that it can be moved up and down.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56071686A JPS5930653B2 (en) | 1981-05-13 | 1981-05-13 | Microwave heating denitrification equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56071686A JPS5930653B2 (en) | 1981-05-13 | 1981-05-13 | Microwave heating denitrification equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57188417A JPS57188417A (en) | 1982-11-19 |
| JPS5930653B2 true JPS5930653B2 (en) | 1984-07-28 |
Family
ID=13467682
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56071686A Expired JPS5930653B2 (en) | 1981-05-13 | 1981-05-13 | Microwave heating denitrification equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5930653B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9700984B2 (en) | 2010-09-17 | 2017-07-11 | Ntn Corporation | Processing method |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59116588A (en) * | 1982-12-24 | 1984-07-05 | 動力炉・核燃料開発事業団 | Heating container for microwave heating denitration device |
| JPH0795111B2 (en) * | 1985-10-01 | 1995-10-11 | 動力炉・核燃料開発事業団 | Microwave heating denitration method and device |
| CA2060931C (en) * | 1992-02-10 | 1996-12-17 | J. R. Jocelyn Pare | Microwave-assisted generation of volatiles, of supercritical fluid, and apparatus therefor |
| FR2727328A1 (en) * | 1994-11-25 | 1996-05-31 | Rhone Poulenc Chimie | Oxidn. or thermo-hydrolysis of chemical element esp. rare earths by microwave heating |
| CN112875770A (en) * | 2020-12-22 | 2021-06-01 | 中国原子能科学研究院 | Microwave denitration device |
-
1981
- 1981-05-13 JP JP56071686A patent/JPS5930653B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9700984B2 (en) | 2010-09-17 | 2017-07-11 | Ntn Corporation | Processing method |
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| Publication number | Publication date |
|---|---|
| JPS57188417A (en) | 1982-11-19 |
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