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JPH0472907B2 - - Google Patents
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JPH0472907B2 - - Google Patents

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Publication number
JPH0472907B2
JPH0472907B2 JP58248501A JP24850183A JPH0472907B2 JP H0472907 B2 JPH0472907 B2 JP H0472907B2 JP 58248501 A JP58248501 A JP 58248501A JP 24850183 A JP24850183 A JP 24850183A JP H0472907 B2 JPH0472907 B2 JP H0472907B2
Authority
JP
Japan
Prior art keywords
gas
guide tube
manufacturing
dissociation
ammonia gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP58248501A
Other languages
Japanese (ja)
Other versions
JPS60135563A (en
Inventor
Makoto Kasai
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Original Assignee
Tokyo Shibaura Electric Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tokyo Shibaura Electric Co Ltd filed Critical Tokyo Shibaura Electric Co Ltd
Priority to JP58248501A priority Critical patent/JPS60135563A/en
Publication of JPS60135563A publication Critical patent/JPS60135563A/en
Publication of JPH0472907B2 publication Critical patent/JPH0472907B2/ja
Granted legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21CNUCLEAR REACTORS
    • G21C17/00Monitoring; Testing ; Maintaining
    • G21C17/10Structural combination of fuel element, control rod, reactor core, or moderator structure with sensitive instruments, e.g. for measuring radioactivity, strain
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C8/00Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/04Treatment of selected surface areas, e.g. using masks
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Plasma & Fusion (AREA)
  • General Engineering & Computer Science (AREA)
  • High Energy & Nuclear Physics (AREA)
  • Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)
  • Monitoring And Testing Of Nuclear Reactors (AREA)

Description

【発明の詳細な説明】 〔発明の技術分野〕 この発明は原子炉計測素子用案内管の製造方法
および製造装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method and apparatus for manufacturing a guide tube for a nuclear reactor measurement element.

〔背景技術およびその問題点〕[Background technology and its problems]

例えば沸騰水形原子炉においては、第1図に示
すように原子炉圧力容器11内に燃料集合体12
および冷却水13が容れられ、各部の中性子検出
あるいは炉内温度検出のために複数組の中性子検
出器集合体14(1組のみ図示)が設置される。
このため集合体14には複数個の中性子検出器1
5,15…が挿入されている。すなわち集合体1
4は第2図および第3図に示すように保護管16
の内部に複数の中性子検出器15,15…および
その出力リード17,17…が挿通され、さらに
この発明の対象である案内管18が挿入されてい
る。この案内管18は径小長尺のステンレス鋼の
パイプからなり、原子炉の運転にあたつて各中性
子検出器の検出性能を校正する目的で校正用の計
測素子(図示せず)をその内部に通すためのもの
である。これは、校正用計測素子をくり返し挿
入、引抜きするため、その内面に第4図に示すよ
うに窒化鋼の層19が形成されている。この窒化
層19は、案内管の全長にわたつて十分な硬度
と、とくに全体にわたつて均一な層厚で形成され
ていなければならない。なぜならば、層が全体的
に或いは部分的に薄すぎると耐摩耗性の点で寿命
が短くなり、また逆に厚すぎると脆弱となり、い
ずれの場合も信頼性の乏しいものとなる。案内管
は例えば、内直径寸法が7mm、肉厚が1.5mm、全
長が14mという、径小で長尺のステンレス鋼パイ
プで形成される。そしてこの案内管を高温に加熱
しつつアンモニアガスを通して窒化層を形成す
る。生成される窒化層の厚さは処理温度、時間、
およびアンモニアガスの解離度に依存する。上記
のように案内管は径小で長尺であるため、温度を
全体にわたつて均一に保つこと、またアンモニア
ガスを全体に均一に接触させることは容易なく、
さらにまたガスの解離度を均一に保つことも容易
ではない。このような事情のため案内管の内面窒
化層の厚さを高硬度で均一に形成することは困難
であつた。
For example, in a boiling water reactor, a fuel assembly 12 is placed in a reactor pressure vessel 11 as shown in FIG.
A plurality of sets of neutron detector assemblies 14 (only one set is shown) are installed to detect neutrons or reactor temperature in each part.
Therefore, the aggregate 14 includes a plurality of neutron detectors 1.
5, 15... are inserted. That is, aggregate 1
4 is a protection tube 16 as shown in FIGS. 2 and 3.
A plurality of neutron detectors 15, 15, . . . and their output leads 17, 17, . This guide tube 18 is made of a long stainless steel pipe with a small diameter, and a calibration measuring element (not shown) is installed inside it for the purpose of calibrating the detection performance of each neutron detector during operation of the nuclear reactor. It is for passing through. Since the calibration measuring element is repeatedly inserted and extracted, a layer 19 of nitrided steel is formed on the inner surface of the measuring element as shown in FIG. This nitrided layer 19 must have sufficient hardness over the entire length of the guide tube and, in particular, must have a uniform layer thickness over the entire length. This is because if the layer is too thin in whole or in part, the lifetime will be shortened in terms of wear resistance, and if it is too thick, it will be brittle, and in either case it will be unreliable. The guide tube is formed of a long stainless steel pipe with a small diameter, for example, having an inner diameter of 7 mm, a wall thickness of 1.5 mm, and a total length of 14 m. Ammonia gas is then passed through the guide tube while heating it to a high temperature to form a nitrided layer. The thickness of the nitride layer produced depends on the processing temperature, time,
and depends on the degree of dissociation of ammonia gas. As mentioned above, since the guide tube is small in diameter and long, it is difficult to maintain a uniform temperature throughout and to bring ammonia gas into uniform contact with the entire area.
Furthermore, it is not easy to maintain a uniform degree of gas dissociation. Due to these circumstances, it has been difficult to form the inner nitrided layer of the guide tube with high hardness and uniform thickness.

〔発明の目的〕[Purpose of the invention]

この発明は、案内管の内面に全体にわたつて所
望の厚さで均一な質の窒化層を能率よく形成し
て、信頼性の高い原子炉計測素子用の案内管を製
造する方法、およびこの方法の実施に直接使用す
る製造装置を提供するものである。
The present invention provides a method for manufacturing a highly reliable guide tube for a nuclear reactor measurement element by efficiently forming a nitride layer of a desired thickness and uniform quality over the entire inner surface of the guide tube, and It provides manufacturing equipment for direct use in carrying out the method.

〔発明の概要〕[Summary of the invention]

この発明の製造方法の特徴は、案内管を高温に
加熱するとともにアンモニアガスを案内管の両開
口端の一方から他方に交互に複数回流通方向を変
えて導入、排出させ窒化層を形成する点にある。
さらにまた、案内管を所定の高温度に保持すると
ともに、その間のアンモニアガスの解離度を20%
乃至45%の範囲内に制御して処理することも一特
徴としている。
The manufacturing method of the present invention is characterized in that the guide tube is heated to a high temperature and ammonia gas is introduced and discharged from one of the open ends of the guide tube to the other by alternating the flow direction multiple times to form a nitrided layer. It is in.
Furthermore, while maintaining the guide tube at a predetermined high temperature, the degree of dissociation of ammonia gas during that time is reduced by 20%.
Another feature is that it can be controlled within a range of 45%.

またこの発明の製造装置は、径小長尺の複数本
の被処理案内管を収容する加熱炉と、案内管の両
端に共通に接続される一対のマニホールドと、こ
れら各マニホールドに各々接続されたガス導入パ
イプおよびガス排出パイプと、これら各パイプへ
のガス導入、排出を切換える如く接続された一対
の切換バルブと、ガス導入用切換バルブの上流に
圧力制御バルブを介して接続されたアンモニアガ
ス源と、上記ガス排出用切換バルブの下流に接続
されアンモニアガスの解離度を検出するガス分析
計とを具備してなることを特徴としている。
Further, the manufacturing apparatus of the present invention includes a heating furnace that accommodates a plurality of small-diameter and long guide tubes to be treated, a pair of manifolds commonly connected to both ends of the guide tubes, and a plurality of manifolds connected to each of these manifolds. A gas introduction pipe, a gas discharge pipe, a pair of switching valves connected to switch gas introduction and discharge to each of these pipes, and an ammonia gas source connected upstream of the gas introduction switching valve via a pressure control valve. and a gas analyzer connected downstream of the gas discharge switching valve to detect the degree of dissociation of ammonia gas.

これによつて所望の厚さで且つ全体にわたつて
比較的均一な窒化層を形成でき、信頼性の高い案
内管を得ることができる。
As a result, a nitrided layer having a desired thickness and being relatively uniform over the entire area can be formed, and a highly reliable guide tube can be obtained.

〔発明の実施例〕[Embodiments of the invention]

以下第5図および第6図を参照してこの発明の
実施例を説明する。なお、同一部分は同一符号で
あらわす。
Embodiments of the present invention will be described below with reference to FIGS. 5 and 6. Note that the same parts are represented by the same symbols.

まずこの発明の製造方法の実施に直接使用する
製造装置の構成を第5図により説明する。この装
置は長い電熱炉21を有し、その両端部に一対の
マニホールド22,23を有し、これらマニホー
ルドに被処理ステンレス鋼長尺案内管18が複数
本接続される。マニホールド22,23にはガス
導入管24a,24bおよび排出管25a,25
bがそれぞれ接続されている。ガス導入径路につ
いて述べると、アンモニアガス(NH3)ガス源
26は、バルブ27、電磁バルブ28、圧力制御
バルブ29、流量計30、逆止弁31を経て電磁
切換バルブ32,33に接続されている。また、
窒素N2のような不活性ガス源34は、バルブ3
5、電磁バルブ36、流量計37逆止弁38を介
して同じく切換バルブ32,33に接続されてい
る。切換バルブの一方32は一方のマニホールド
22に、他方のバルブ33は他方のマニホールド
23にそれぞれガス導入管24a,24bを介し
て接続されている。なお図中の符号Gは圧力計を
あらわし、ガス管径路に示した矢印はガスの流れ
方向をあらわしている。各マニホールド22,2
3のガス排出管25a,25bは、もう1組の電
磁切換バルブ39,40に接続され、その出口は
電磁バルブ41、流量計42、ガス分析計43、
電磁バルブ44を介してガス排出器すなわちスク
ラバ45に接続されている。また切換バルブ2
9,40の出口は、バイパス用のバルブ46を介
してバイパス路からスクラバ45へ通じており、
さらにバルブ47を介してビユーレツト48を介
して同じくスクラバ45に接続されている。なお
符号53は水タンク、49は水バルブをあらわ
し、いずれもビユーレツト48に付属している。
このビユーレツト48、およびガス分析計43
は、被処理案内管を通つて出てきたアンモニアガ
スの解離度を測定するものであり、分析計43の
出力信号はレコーダ50に自動記録され、また同
じくこの出力信号は圧力制御器51に与えられ、
この制御器51はNH3ガス源経路の圧力制御バ
ルブ29の圧力を自動制御するようになつてい
る。切換バルブ32,33,39,40は、切換
制御器52により、導入ガスがマニホールドから
被処理案内管18に流れる方向を図の左、右方向
に自動的に切換える。すなわち切換バルブ32か
ら導入パイプ24a、図の左のマニホールド22
から案内管を通り、図の右のマニホールド23を
通つて排出管25bを経て切換バルブ40を通り
排出経路に至る順路と、この順路を遮断するとと
もに切換バルブ33から導入管24b、図の右側
のマニホールド23、案内管、左のマニホールド
22、排出管25a、切換バルブ39を通る順路
とが、各切換バルブの電磁コイルへの通電制御に
よつて切換えるものである。
First, the configuration of a manufacturing apparatus directly used for carrying out the manufacturing method of the present invention will be explained with reference to FIG. This apparatus has a long electric heating furnace 21, and a pair of manifolds 22, 23 at both ends thereof, to which a plurality of long stainless steel guide tubes 18 to be treated are connected. The manifolds 22 and 23 have gas introduction pipes 24a and 24b and discharge pipes 25a and 25.
b are connected to each other. Regarding the gas introduction path, an ammonia gas (NH 3 ) gas source 26 is connected to electromagnetic switching valves 32 and 33 via a valve 27, an electromagnetic valve 28, a pressure control valve 29, a flow meter 30, and a check valve 31. There is. Also,
An inert gas source 34, such as nitrogen N2 , is supplied to the valve 3.
5. Also connected to switching valves 32 and 33 via an electromagnetic valve 36, a flow meter 37 and a check valve 38. One of the switching valves 32 is connected to one manifold 22, and the other valve 33 is connected to the other manifold 23 via gas introduction pipes 24a and 24b, respectively. Note that the symbol G in the figure represents a pressure gauge, and the arrow shown on the gas pipe path represents the flow direction of gas. Each manifold 22, 2
The gas exhaust pipes 25a, 25b of No. 3 are connected to another set of electromagnetic switching valves 39, 40, and the outlets thereof are connected to an electromagnetic valve 41, a flow meter 42, a gas analyzer 43,
It is connected via a solenoid valve 44 to a gas exhauster or scrubber 45 . Also, switching valve 2
The outlets 9 and 40 communicate from the bypass path to the scrubber 45 via a bypass valve 46,
Furthermore, it is also connected to a scrubber 45 via a valve 47 and a brewet 48. Note that the reference numeral 53 represents a water tank and 49 represents a water valve, both of which are attached to the brewet 48.
This filter 48 and gas analyzer 43
is for measuring the degree of dissociation of ammonia gas coming out through the guide tube to be treated, and the output signal of the analyzer 43 is automatically recorded on the recorder 50, and this output signal is also given to the pressure controller 51. is,
This controller 51 is designed to automatically control the pressure of the pressure control valve 29 in the NH 3 gas source path. The switching valves 32, 33, 39, and 40 automatically switch the direction in which the introduced gas flows from the manifold to the treated guide tube 18 to the left or right in the figure by the switching controller 52. That is, from the switching valve 32 to the introduction pipe 24a, the manifold 22 on the left side of the figure.
From the guide pipe, through the manifold 23 on the right side of the figure, through the discharge pipe 25b, and through the switching valve 40 to the exhaust route, and while blocking this route, from the switching valve 33 to the inlet pipe 24b, on the right side of the figure. The route passing through the manifold 23, the guide pipe, the left manifold 22, the discharge pipe 25a, and the switching valve 39 is switched by controlling the energization of the electromagnetic coil of each switching valve.

次に、第6図をも参照しながら処理手順を説明
する。まず第6図に符号aで示す工程すなわち被
処理案内管の両端をマニホールドに接続して電熱
炉内に装着し、炉温を上げる前に案内管の内部に
NH3ガスを十分流し、内部の空気を排出してガ
ス置換する工程からはじめる。同図において実線
曲線(NH3)がアンモニアガスの流量をあらわ
している。この工程aのあと、NH3ガスの流量
を低減し、電熱炉の温度を上昇させ案内管の温度
Tを上昇させてゆく工程bにすすむ。なおこの温
度上昇途中において案内管の内表面酸化層の除去
のためHN3ガスを微量流しながらマニホールド
内に塩化ビニール系樹脂のビーズを投入しその気
化ガスを案内管に通す。この工程bの後段で炉内
温度を一定に保持して案内管の温度の均一化をは
かる。次に工程cにおいて温度をさらに上げつつ
NH3ガスの流量を一気に増加し、窒化処理をは
じめる。すなわちNH3ガスが高温分解に適する
温度に保ちながら工程dでNH3ガスの流量を制
御しつつ装置の切換制御器52により各切換バル
ブを切換え動作させて所定時間ごとにNH3ガス
の流れ方向を交互に切換える。例えばNH3ガス
の流れ方向を5分ごとに逆転させ、5〜20回、自
動的にくり返す。その間、装置のガス分析計43
あるいはビユーレツト48による排出経路の
NH3ガスの解離度(2NH3→3H2+2N)を検出
し、その解離度に応じて圧力制御器51および圧
力制御バルブ29を制御して導入NH3ガスの流
量を制御する。この制御領域を第6図に斜線領域
Pであらわしている。例えば解離度が20%以下と
いう低い場合には圧力制御バルブ29を締めてゆ
き流量を減らし、解離度が上昇するように制御す
る。また逆に排出NH3ガスの解離度が45%以上
という高い場合はNH3導入ガス流量を増加して
解離度が低下してゆくように制御する。そしてこ
の工程の間、好ましくは解離度が20%乃至45%の
範囲内になるように制御される。こうして所定時
間処理したのち炉温を降下させると同時にNH3
ガスの導入を停止し、引き続いて案内管の酸化防
止のためN2ガスを導入しつつ徐冷する工程eに
移る。
Next, the processing procedure will be explained with reference to FIG. First, in the step shown by symbol a in Fig. 6, both ends of the guide tube to be treated are connected to a manifold and installed in an electric heating furnace, and before raising the furnace temperature, the inside of the guide tube is
Start by flowing sufficient NH 3 gas to exhaust the internal air and replace the gas. In the figure, the solid line curve (NH 3 ) represents the flow rate of ammonia gas. After step a, proceed to step b, in which the flow rate of NH 3 gas is reduced, the temperature of the electric furnace is increased, and the temperature T of the guide tube is increased. During this temperature rise, beads of vinyl chloride resin are introduced into the manifold while a small amount of HN 3 gas is flowed in order to remove the oxidized layer on the inner surface of the guide tube, and the vaporized gas is passed through the guide tube. At the latter stage of step b, the temperature inside the furnace is kept constant to make the temperature of the guide tube uniform. Next, in step c, the temperature is further increased.
The flow rate of NH 3 gas is increased all at once and the nitriding process begins. That is, while maintaining the NH 3 gas at a temperature suitable for high-temperature decomposition, the flow rate of the NH 3 gas is controlled in step d, and each switching valve is operated by the switching controller 52 of the device to change the flow direction of the NH 3 gas at predetermined time intervals. Switch alternately. For example, the flow direction of NH 3 gas is reversed every 5 minutes, and the process is automatically repeated 5 to 20 times. Meanwhile, the device's gas analyzer 43
Alternatively, the discharge route by the brewet 48
The degree of dissociation of NH 3 gas (2NH 3 →3H 2 +2N) is detected, and the pressure controller 51 and pressure control valve 29 are controlled according to the degree of dissociation to control the flow rate of the introduced NH 3 gas. This control area is represented by a hatched area P in FIG. For example, when the degree of dissociation is low, such as 20% or less, the pressure control valve 29 is tightened to reduce the flow rate, thereby controlling the degree of dissociation to increase. Conversely, if the degree of dissociation of the discharged NH 3 gas is as high as 45% or more, the flow rate of the NH 3 introduced gas is increased to control the degree of dissociation to decrease. During this step, the degree of dissociation is preferably controlled within the range of 20% to 45%. After processing in this way for a predetermined period of time, the furnace temperature is lowered and at the same time NH 3
The introduction of gas is stopped, and then the process moves to step e, in which N2 gas is introduced to prevent the guide tube from oxidizing, and the guide tube is slowly cooled.

以上の処理によつて案内管の内面に好ましくは
60μm〜70μmの厚さの窒化鋼の層を形成すること
ができる。なおこの発明の装置において各バルブ
等は以上の処理を行なうように制御され、またガ
ス分析計に並列に設けられたバイパス経路は、分
析計へのガス流量が計測精度を最適とする量に設
定するための径路である。またビユーレツトは計
測の校正のためなどに用い、総合的なガス分析精
度を高め、維持するのにも有効である。勿論
NH3源からの流量制御は手動で行なうこともで
き、あるいは前述の如く自動制御とすることもで
きる。
Through the above treatment, the inner surface of the guide tube is preferably
A layer of nitrided steel with a thickness of 60 μm to 70 μm can be formed. In the device of this invention, each valve etc. is controlled to perform the above processing, and the bypass path provided in parallel to the gas analyzer is set to an amount that optimizes the measurement accuracy of the gas flow rate to the analyzer. It is a route for Biurets are also used to calibrate measurements and are effective in increasing and maintaining overall gas analysis accuracy. Of course
Control of the flow rate from the NH 3 source can be done manually or automatically as described above.

〔発明の効果〕〔Effect of the invention〕

この発明の製造方法は、アンモニアガスを高温
で分解し径小長尺の案内管に流れ方向を交互に切
り換えて複数回くり返しながら窒化処理するた
め、例えば内直径が7mmで長さが14mというよう
な案内管でも、窒化鋼層の厚さのばらつきをわず
かなものとし、再現性よく製造することができ
る。とくに解離度を20%〜45%の範囲内に制御し
て処理することにより、硬度のすぐれた所定膜厚
の窒化層をせいぜい30分〜1時間の窒化処理(工
程d)により得ることができる。
The manufacturing method of this invention decomposes ammonia gas at high temperature and performs nitriding treatment by alternating the flow direction in a small diameter and long guide tube and repeating the process several times. Even in the case of a guide tube, the variation in the thickness of the nitrided steel layer is minimized, and it can be manufactured with good reproducibility. In particular, by controlling the degree of dissociation within the range of 20% to 45%, a nitrided layer with excellent hardness and a predetermined thickness can be obtained by nitriding for at most 30 minutes to 1 hour (step d). .

またこの発明の装置により、自動的に上記製造
方法を確実に実施でき、高能率に、且つ安定に処
理できる。
Further, with the apparatus of the present invention, the above manufacturing method can be carried out automatically and reliably, and processing can be performed with high efficiency and stability.

このように原子炉用部材として信頼性の高い案
内管を製造することができる。
In this way, a highly reliable guide tube can be manufactured as a member for a nuclear reactor.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は原子炉の概略構成図、第2図はその検
出器集合体の縦断面図、第3図は第2図の3−3
における横断面図、第4図はその案内管の拡大横
断面図、第5図はこの発明の装置の実施例を示す
構成系統図、第6図はこの発明の製造方法の実施
例の工程における温度、ガス流量制御曲線図であ
る。 18…案内管、19…窒化層、21…電熱炉、
22,23…マニホールド、32,33,39,
40…切換制御バルブ、26…アンモニアガス
源、29…圧力制御バルブ、43…ガス分析計、
48…ビユーレツト、51…圧力制御器。
Figure 1 is a schematic configuration diagram of the reactor, Figure 2 is a vertical cross-sectional view of its detector assembly, and Figure 3 is 3-3 in Figure 2.
FIG. 4 is an enlarged cross-sectional view of the guide tube, FIG. 5 is a structural diagram showing an embodiment of the apparatus of the present invention, and FIG. 6 is a diagram showing the steps of an embodiment of the manufacturing method of the present invention. It is a temperature and gas flow rate control curve diagram. 18... Guide tube, 19... Nitrided layer, 21... Electric heating furnace,
22, 23...manifold, 32, 33, 39,
40...Switching control valve, 26...Ammonia gas source, 29...Pressure control valve, 43...Gas analyzer,
48...Biuret, 51...Pressure controller.

Claims (1)

【特許請求の範囲】 1 ステンレス鋼からなる径小長尺の原子炉計測
素子用案内管の内面に窒化層を形成する製造方法
において、上記案内管を高温に加熱するとともに
アンモニアガスを案内管の両開口端の一方から他
方に交互に複数回流通方向を変えて導入、排出さ
せ窒化層を形成することを特徴とする原子炉計測
素子用案内管の製造方法。 2 案内管を所定の高温度に保持するとともに、
その間のアンモニアガスの解離度を20%乃至45%
の範囲内に制御して処理する特許請求の範囲第1
項記載の製造方法。 3 径小長尺の複数本の原子炉計測素子用案内管
を収容する加熱炉と、上記案内管の両端に共通に
接続される一対のマニホールドと、これら各マニ
ホールドに各々接続されたガス導入パイプおよび
ガス排出パイプと、これら各パイプへのガス導
入、排出を切換える如く接続された一対の切換バ
ルブと、ガス導入用切換バルブの上流に圧力制御
バルブを介して接続されたアンモニアガス源と、
上記ガス排出用切換バルブの下流に接続されたア
ンモニアガスの解離度を検出するガス分析計とを
具備してなる原子炉計測素子用案内管の製造装
置。
[Claims] 1. A manufacturing method for forming a nitrided layer on the inner surface of a small diameter and long guide tube for a nuclear reactor measurement element made of stainless steel, in which the guide tube is heated to a high temperature and ammonia gas is added to the guide tube. A method for manufacturing a guide tube for a nuclear reactor measurement element, characterized by forming a nitrided layer by introducing and discharging the flow direction from one of both open ends to the other by alternating the flow direction a plurality of times. 2 While maintaining the guide tube at a predetermined high temperature,
The degree of dissociation of ammonia gas between 20% and 45%
Claim 1 of controlling and processing within the scope of
Manufacturing method described in section. 3. A heating furnace that accommodates a plurality of small-diameter and long guide tubes for reactor measurement elements, a pair of manifolds commonly connected to both ends of the guide tubes, and gas introduction pipes connected to each of these manifolds, respectively. and a gas discharge pipe, a pair of switching valves connected to switch gas introduction and discharge to each of these pipes, and an ammonia gas source connected upstream of the gas introduction switching valve via a pressure control valve;
A manufacturing apparatus for a guide tube for a nuclear reactor measurement element, comprising: a gas analyzer connected downstream of the gas discharge switching valve for detecting the degree of dissociation of ammonia gas.
JP58248501A 1983-12-24 1983-12-24 Method and device for producing guide pipe for measuring element of nuclear reactor Granted JPS60135563A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58248501A JPS60135563A (en) 1983-12-24 1983-12-24 Method and device for producing guide pipe for measuring element of nuclear reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58248501A JPS60135563A (en) 1983-12-24 1983-12-24 Method and device for producing guide pipe for measuring element of nuclear reactor

Publications (2)

Publication Number Publication Date
JPS60135563A JPS60135563A (en) 1985-07-18
JPH0472907B2 true JPH0472907B2 (en) 1992-11-19

Family

ID=17179107

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58248501A Granted JPS60135563A (en) 1983-12-24 1983-12-24 Method and device for producing guide pipe for measuring element of nuclear reactor

Country Status (1)

Country Link
JP (1) JPS60135563A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03111552A (en) * 1989-09-26 1991-05-13 Osaka Oxygen Ind Ltd Metal tube oxidation treatment equipment

Also Published As

Publication number Publication date
JPS60135563A (en) 1985-07-18

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