[go: up one dir, main page]

JP2004075884A - Rare earth oxysulfide ceramic regenerator material, method for producing the same, and cryogenic regenerator using the regenerator material - Google Patents

Rare earth oxysulfide ceramic regenerator material, method for producing the same, and cryogenic regenerator using the regenerator material Download PDF

Info

Publication number
JP2004075884A
JP2004075884A JP2002239192A JP2002239192A JP2004075884A JP 2004075884 A JP2004075884 A JP 2004075884A JP 2002239192 A JP2002239192 A JP 2002239192A JP 2002239192 A JP2002239192 A JP 2002239192A JP 2004075884 A JP2004075884 A JP 2004075884A
Authority
JP
Japan
Prior art keywords
rare earth
particles
earth oxysulfide
regenerator
primary particles
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.)
Granted
Application number
JP2002239192A
Other languages
Japanese (ja)
Other versions
JP4170703B2 (en
Inventor
Takakimi Yanagiya
柳谷 高公
Toshiteru Nozawa
野沢 星輝
Katsunori Kagawa
香川 克典
Atsushi Ono
小野 淳
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.)
Konoshima Chemical Co Ltd
Original Assignee
Konoshima Chemical 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 Konoshima Chemical Co Ltd filed Critical Konoshima Chemical Co Ltd
Priority to JP2002239192A priority Critical patent/JP4170703B2/en
Publication of JP2004075884A publication Critical patent/JP2004075884A/en
Application granted granted Critical
Publication of JP4170703B2 publication Critical patent/JP4170703B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Compositions Of Oxide Ceramics (AREA)
  • Porous Artificial Stone Or Porous Ceramic Products (AREA)

Abstract

【構成】GdS等の希土類オキシ硫化物の結晶粒子を1次粒子とし、この1次粒子がネックで互いに焼結された多孔質体を構成粒子とする。このような構成粒子を得るには、顆粒状の希土類オキシ硫化物を1150〜1350℃でHIP焼成し、比較的低温でHIP焼成することにより、1次粒子の粒成長や構成粒子の緻密化を抑制しながら、1次粒子間のネックを成長させると良い。
【効果】冷凍機の運転中の構成粒子の破壊や微粉の発生が少なく、しかも冷凍能力の高いセラミックス蓄冷材が得られる。
【選択図】      図1
[Constitution] Crystal particles of rare earth oxysulfide such as Gd 2 O 2 S are used as primary particles, and a porous body in which the primary particles are sintered together at a neck is used as a constituent particle. In order to obtain such constituent particles, granular rare earth oxysulfide is HIP-baked at 1150 to 1350 ° C. and HIP-baked at a relatively low temperature so that the primary particles grow and the constituent particles are densified. It is preferable to grow the neck between the primary particles while suppressing.
[Effect] A ceramic regenerator material having a high refrigerating capacity with less destruction of constituent particles and generation of fine powder during operation of the refrigerator can be obtained.
[Selection diagram] Fig. 1

Description

【0001】
【発明の技術分野】
本発明は、一般式 RS (Rは Yを含むLa, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy,Ho, Er, Tm, Yb及びLuから選択される少なくとも1種類の希土類元素を表す。)で表せられる希土類オキシ硫化物蓄冷材とその製造方法、並びにこの蓄冷材を用いた蓄冷器に関するものである。さらに詳しくは、冷凍機運転中において、微粉化する恐れが少なく、耐久性に優れ、極低温領域における冷凍能力に優れた蓄冷材やその製造方法、及びそれを用いた蓄冷器に関する。
【0002】
【従来の技術とその課題】
超伝導磁石やセンサーなどの冷却には、液体ヘリウムが不可欠で、ヘリウムガスの液化には、膨大な圧縮仕事が必要であり、そのため大型な冷凍機が必要となる。しかしリニアモーターカーやMRI(磁気共鳴診断装置)などの超伝導現象を利用した小型装置に、大型の冷凍機を使用することは難しい。そのため液体ヘリウム温度(4.2K)が発生可能な小型で高性能の冷凍機の開発が不可欠である。このような冷凍機には、軽量・小型で熱効率が優れていることが要求されている。例えば超伝導MRI装置等においては、例えばGM冷凍機(ギフォード・マクマホン型の小型ヘリウム冷凍機)が用いられている。このGM冷凍機は、主としてHeガス等の作動媒質を圧縮するコンプレッサ、圧縮した作動媒質を膨張させる膨張部、及び膨張部で冷却させた作動媒質の冷却状態を維持するための極低温蓄冷器で構成されている。そして1分間に約60回のサイクルで、コンプレッサによって圧縮された作動媒質を冷凍機で膨張させて冷却し、冷凍機の膨張部の先端部を通じて、被冷却系を冷却する。
【0003】
小型冷凍機の冷却能力や最低到達温度は、冷凍機に組み込まれている蓄冷材に依存し、蓄冷材は大きな熱容量をもち、かつ熱交換効率が高い必要がある。Pbなどの在来の金属蓄冷材では、10K以下の低温で熱容量が急激に低下する。そこで、液化ヘリウム温度(4.2K)付近まで大きな熱容量を有するHoCuやErNiなどの希土類金属間化合物蓄冷材が開発された(特許2609747号)。しかし希土類金属間化合物蓄冷材は、7K以下で熱容量が大きく低下し、4.2K付近の極低温領域での熱容量は0.3J/cc・K未満となる。極低温領域での冷凍能力を十分保持するには、その温度での蓄冷材の熱容量0.3J/cc・K以上必要で、HoCuゃErNiなどの希土類金属間化合物の蓄冷材は極低温領域での冷凍能力が不十分である。また希土類金属間化合物は極めて高価であり、これを数百グラムオーダーで使用する蓄冷材も極めて高価になる。
【0004】
希土類金属間化合物蓄冷材は、特許2609747号などに開示されるように、金属溶湯を急冷凝固して調製され、当然のことながら中実の緻密な粒体で、平均粒径は0.01〜3mm程度である。粒体の平均粒径を大きくすると、Heガスの通気抵抗は減少するが、熱交換効率は低下し、平均粒径を小さくすると熱交換効率は向上するものの、通気抵抗が激増する。
【0005】
希土類金属間化合物の粒体を互いに固定して、蓄冷材の強度を増すとともに、通気性を向上させることも検討されている。例えば特開平11−264618号は、希土類金属間化合物の粒体表面に、Pb,In,Sn等の低融点金属をコーティングし、液相焼結によって粒体を互いに固定化することを提案している。しかしながら微細な希土類金属間化合物の粒体を得ることは困難で、粒体の平均粒径は例えば100〜250μmとされ、平均粒径が大きいため、熱交換効率には限界がある。
【0006】
【発明の課題】
本発明の課題は、冷凍機の冷凍能力を向上させるために、
・ 高圧Heガスの通気性の向上と圧力損失の軽減を可能とし、
・ 冷凍機の稼動中による高圧Heガス等の作動媒質の往復運動による振動や衝撃、あるいは蓄冷器の内部を通過する高圧Heガスによる流体力学的な応力に十分に耐え、
・ 極低温領域において優れた冷凍能力を長時間保持することが可能な希土類オキシ硫化物セラミックス蓄冷材とその製造方法、及び蓄冷器を提供することにある。
【0007】
【発明の構成】
本発明の希土類オキシ硫化物セラミックス蓄冷材は、
一般式 RS (RはYを含むLa, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm,Yb及びLuから選択される少なくとも1種類の希土類元素を表す。) で表される希土類オキシ硫化物を用いた蓄冷材において、
前記希土類オキシ硫化物の結晶粒子を1次粒子とし、該1次粒子がネックで互いに焼結された多孔質体を構成粒子とすることを特徴とする(請求項1)。
【0008】
好ましくは、前記結晶粒子の平均結晶粒径を0.2〜5μm、より好ましくは0.5〜3μm、最も好ましくは0.9〜2μmとする(請求項2)。
【0009】
また多孔質体の相対密度は、好ましくは60〜85%とし、より好ましくは65〜80%、最も好ましくは70〜75%とする(請求項3)。
【0010】
希土類オキシ硫化物の構成希土類元素は任意であるが、希土類金属間化合物よりも低温側の4〜7K程度に比熱のピーク温度を有し、液体ヘリウム温度への冷却に適したGdやTb、あるいは2〜4K程度に比熱のピーク温度を有し、液体ヘリウム温度よりもさらに低温への冷却に適したDyやHo等が好ましい。希土類オキシ硫化物蓄冷材では構成希土類元素を1種類とする必要はなく、例えばGdTb2−xSのように、2種類以上の構成希土類元素を用いても良い。好ましくは希土類オキシ硫化物での構成希土類元素の80原子%以上を、Gd,Tb,Dy,またはHoとする(請求項4)。
【0011】
本発明の希土類オキシ硫化物セラミックス蓄冷材の製造方法は、
一般式 RS (RはYを含むLa, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm,Yb及びLuから選択される少なくとも1種類の希土類元素を表す。)で表される希土類オキシ硫化物を用いた蓄冷材の製造方法において、
前記希土類オキシ硫化物の粉体を顆粒に造粒し、
該顆粒を1150〜1350℃でHIP焼成して、希土類オキシ硫化物の結晶粒子を1次粒子とし、該1次粒子がネックで互いに焼結された多孔質体からなる蓄冷材とすることを特徴とする(請求項5)。
【0012】
HIP温度はより好ましくは、1200〜1300℃とする。
また好ましくは、HIPでの圧力を50〜200MPa,焼成時間を1〜10時間とする(請求項6)。
【0013】
本発明の極低温蓄冷器は、請求項1〜4のいずれかの希土類オキシ硫化物セラミックス蓄冷材を用いたものである(請求項7)。
【0014】
【発明の作用と効果】
本発明の希土類オキシ硫化物セラミックス蓄冷材では、結晶粒子からなる1次粒子をネックで互いに焼結した多孔質体(2次粒子)を構成粒子とする。セラミックスでは、1次粒子の粒径を例えば0.2〜5μm程度と極く小さくできる。このため、多孔質体の内部をHeガスが流れて1次粒子と熱交換するので、熱交換効率を向上できる。微細な1次粒子はネックで互いに焼結され、多孔質体全体としては強度のある材料となる。また1つの1次粒子の中に複数の結晶粒子が存在することも可能ではあるが、1次粒子内で密着した複数の結晶粒子は焼結の過程で融合して、原則として1個の結晶粒子に成長する。
【0015】
このようにして本発明では、構成粒子が多孔質であり、Heガスの通気性が高いため、熱交換効率が高く圧力損失が少ない、蓄冷材や畜冷器が得られる。また本発明の蓄冷材や畜冷器は、1次粒子が互いにネックで焼結されているため、構成粒子の強度が高く、冷凍機での振動や衝撃、応力などに耐えることができ、このため優れた冷凍能力を長時間保持できる(請求項1,請求項7)。これに対して金属の場合、微細な1次粒子の粉体を得ること自体が困難で、1次粒子を互いに焼結して多孔質体としても、1次粒子のサイズが大きいので、熱交換効率の向上は困難である。
【0016】
希土類オキシ硫化物セラミックス蓄冷材での平均結晶粒径は、高圧Heガスの通気性の向上と圧力損失の軽減に関与するため、HIP焼成後の平均結晶粒径で0.2〜5μmが好ましく、より好ましくは0.5〜3μm、さらに好ましくは0.9〜2μmとする。平均結晶粒径が5μmを越えると、高圧Heガスと1次粒子との熱交換効率が低下し、平均結晶粒径が0.2μm未満では、構成粒子内部での高圧Heガスの通気性が著しく低下し、圧力損失が増大する。構成粒子の内部での通気抵抗は粘性抵抗であり、粘性抵抗は高圧Heガスが流れる空隙のサイズに反比例する。そして空隙のサイズは、1次粒子のサイズに比例する。
【0017】
1次粒子の平均結晶粒径には、セラミックスの調製上の制限も加わる。焼結前のセラミックス粉体での1次粒子の粒径を考えると、焼結後の蓄冷材での1次粒子の平均結晶粒径をこれよりも小さくすることは困難で、セラミックス粉体での1次粒子の平均粒径を0.2μmよりも充分小さくすることは、粉体のハンドリング性の点から困難である。このように1次粒子の平均結晶粒径を0.2μm以上とすることには、セラミックス蓄冷材の原料粉末を容易に得うるようにするとの意味もある(請求項2)。
【0018】
希土類オキシ硫化物セラミックス蓄冷材での構成粒子の相対密度は、60〜85%が好ましく、より好ましくは65〜80%とし、さらに好ましくは70〜75%とする。構成粒子の強度は相対密度に依存し、例えば相対密度が50%程度の場合、高圧Heガスの運動による振動や衝撃、応力に耐えることは困難である。構成粒子の強度は相対密度が50〜70%程度の範囲で、相対密度と共に指数的に向上する。一方、構成粒子内の通気性は相対密度と共に急激に低下し、特に相対密度が80%を越えると密度と共に指数的に減少し、相対密度が85%を越えると極端に通気性が低下する。そこで構成粒子の相対密度を60〜85%とすると、構成粒子の強度を確保できると共に、構成粒子内の通気性も確保できる(請求項3)。
【0019】
希土類オキシ硫化物セラミックスでの構成希土類元素をGdやTbとすると、4〜7K程度に比熱のピークが表れ、これは希土類金属間化合物での比熱のピークよりも低く、液体He温度への冷却に適している。なおGdSの比熱のピーク(磁気相転移温度)は5.2K、TbSで6.3Kで、GdTb2−xS(0≦X≦1.8)では4.2〜5.3K程度に比熱のピークが表れる。また希土類オキシ硫化物セラミックス蓄冷材の高温側に希土類金属間化合物蓄冷材を配置すると、液体He温度まで効率的に冷却できる。希土類オキシ硫化物セラミックス蓄冷材の構成希土類元素をDyやHoとすると、DySで比熱のピークは4.6K、HoSで2.2Kとなる。このためGdSやTbS、GdTb2−xS(0<X<2)を高温側に配置し、その低温側にDySやHoSを配置すると、さらに低い温度への冷却が容易になる(請求項4)。
【0020】
本発明の希土類オキシ硫化物蓄冷材を製造するには、例えば原料の希土類酸化物粉末を、加熱下でHS, CHSH等の酸化数−2の硫黄原子を含むガスを流して反応させて、希土類オキシ硫化物粉末を作製し、この粉末を造粒する。あるいは希土類酸化物粉末を造粒した後に、酸化数−2の硫黄原子を含むガスと反応させて希土類オキシ硫化物としても良い。造粒の方法自体は任意で、例えば転動造粒、押し出しと転動造粒との組み合せ、流動造粒、噴霧乾燥造粒、型押し造粒等でも良い。
【0021】
希土類オキシ硫化物セラミックス蓄冷材を得るためには、造粒した粒子をHIP(熱間静水圧)焼成が好ましい。従来の常圧焼成法では、高温焼成を行うと、1次粒子間のネックが成長するが、これと同時に粒成長と緻密化とが生じてしまうため、構成粒子の通気性と強度の双方を確保することができない。一方、粒成長と緻密化とを抑制するために低温焼成を行うと、1次粒子間のネックが成長せず、構成粒子の強度を得ることができない。HIPの焼成雰囲気(圧力媒体)には例えばアルゴン等の不活性ガスを用い、焼成温度は1150〜1350℃、特に1200〜1300℃、焼成時間はピーク温度への保持時間で1〜10時間、圧力は50〜200MPaが好ましい。これらは構成粒子の相対密度を60〜85%とする条件で、実験的に求めたものである。
【0022】
構成粒子を内包する球(外接球)の直径は、通気性と熱交換効率、及び強度に影響し、平均の直径が0.01〜2mmが好ましい。また構成粒子のアスペクト比(長径と短径の比)は3以下が好ましく、より好ましくは2以下とし、特に好ましくは1.2以下とする。これはアスペクト比が小さいほど、均一な充填が容易で、かつ高圧Heガスの運動による振動や衝撃、応力による、微粉の発生が少ないからである。ただし1次粒子自体のアスペクト比は任意であり、構成粒子の内部では非球状の1次粒子を互いに結合して、大きな空隙を得るのが好ましい。
【0023】
本発明の蓄冷器は、上記の希土類オキシ硫化物セラミックス蓄冷材を蓄冷筒に充填したものであるが、例えば複数の層に分割して、層毎に別の蓄冷材を充填しても良い。また希土類オキシ硫化物セラミックス蓄冷材の高温側に、HoCu等の希土類金属間蓄冷材を充填し、高温側から最低到達温度まで連続した比熱を持つようにするのが好ましい。
【0024】
【実施例】
以下に実施例を説明する。
【0025】
【試料1】
酸化ガドリニウムGdの平均粒径は、フィッシャー法により0.46μmであった。この酸化ガドリニウムを石英ボートに充填し、石英反応管に硫化水素ガス H2Sを流しながら、650℃ で反応させる。反応生成物のX線回折を測定したところ、ガドリニウムオキシ硫化物 GdSのみのピークしか認められず、希土類酸化物に対する反応収率は100%であった。得られたGdS粉体(平均粒径0.46μm)を転動造粒した。転動造粒した粉体をアルミナ製のルツボに充填し、HIP焼成を行うため、炉内を十分に真空排気した後に、アルゴンガスを導入し、アルゴン雰囲気中で焼成した。焼成温度を1250℃、圧力を150MPa、焼成時間を5時間にすることによって、相対密度が、ピクノメーター法で理論密度の72%の構成粒子を得た。
【0026】
焼成後の構成粒子とナイロン系メディアと10wt%濃度のアルミナスラリーを加工槽内に装入し、回転バレル加工法による表面加工処理を行った。加工時間を2時間にすると、構成粒子表面に突起物として存在する結晶粒子を除去できた。なお表面状態の観察は走査型電子顕微鏡(SEM)によって行った。表面加工した構成粒子をフィルターネットで篩い分けし、篩い分けをした構成粒子を約25°に傾けた鉄板(鏡面に研磨したもの)上に転がし、転がり落ちた構成粒子を回収して、形状分級を行なった。構成粒子100個に対して、構成粒子を内包する球の直径の平均は0.4mmで、構成粒子の平均アスペクト比は1.1であった。なお、構成粒子の平均粒径及び平均アスペクト比は、ビデオハイスコープシステムを用いて撮影した画像から測定した。形状分級後の構成粒子を試料1とする。
【0027】
構成粒子をプラスチック中に固定し、切断して内部の1次粒子をSEMで観察した。SEM写真を図1に示す。SEMでの観察から構成粒子を構成する結晶粒子の平均粒径は1.1μmであった。また相対密度は前記のように72%であった。結晶粒子は互いにネックで焼結されて固定され、結晶粒子の間には空隙が残され、空隙は連通して開気孔を構成していた。また各構成粒子は互いに癒着していなかった。
【0028】
次に構成粒子の強度を調べるために、100個の構成粒子を一辺が5cmで他辺が10cmの長方形状のビニール袋に入れ、120回/分の振蕩機で5分間振った後に、構成粒子の破砕状況を調べたが、構成粒子の破壊や微粉の発生は確認できなかった。
【0029】
このようにして得られた構成粒子を、GM冷凍機の冷却部にほぼ最密充填で充填した後、熱容量25J/KのHeガスを3g/secの質量流量、16atmのガス圧条件で、GM冷凍運転サイクルを連続1000時間及び3000時間継続した。1000時間及び3000運転後の構成粒子を観察したが、破壊された構成粒子や微粉は観察されなかった。また上記の構成粒子の冷凍特性を消費電力3.4kWの2段式GM冷凍機により調べた。高温側の1段目の蓄冷器にはPbを使用し、2段目の蓄冷器の高温側にHoCuを50vol%、2段目の蓄冷器の低温側に試料1の構成粒子を50vol%装填して、冷凍能力を調べた。4.2Kでの冷凍能力は1.94W、無負荷時の最低到達温度2.62Kであった。そして連続1000時間あるいは3000時間冷凍機を運転しても、冷凍能力や最低到達温度に変化は生じなかった。
【0030】
試料1で転動造粒した顆粒に対して、焼結法や焼結条件を変えて、蓄冷材の強度と冷凍特性とを評価した。試料1で用いたGdSの転動造粒顆粒をアルミナ製ルツボに充填し、常圧のアルゴン雰囲気中で焼成温度を1250℃で5時間焼成した。この試料を試料1と同様に回転バレル加工すると、加工中に多量の微粉が発生したので、蓄冷材として使用できないものとして、それ以上の試験を行わなかった(試料2)。SEMでは、1次粒子と1次粒子との間で僅かにネックが成長している程度であり、ピクノメータ法による2次粒子(焼結された個々の顆粒)の相対密度は52%であった。
【0031】
試料2での焼結温度が低すぎたため、常圧焼結で焼結温度を1350℃、1500℃に変化させた。1350℃焼結では、2次粒子は多孔質であったが、1次粒子間のネックの形成は僅かであり、回転バレル加工で多量の微粉が発生したため、それ以上の評価を行わなかった。1500℃焼結では、2次粒子の相対密度は99.9%、平均結晶粒径は3.2μmであった。この試料を試料1と同様に表面加工と篩い分け及び形状分級を行い、蓄冷材として冷凍機に充填し、1000時間連続で冷凍機を運転した。4.2Kでの冷凍能力は1.69Wで、最低到達温度は2.62Kで、試料1と比較して冷凍能力は85%に低下した。
【0032】
常圧焼結では、多孔質でかつ1次粒子間がネックで結合され、充分なHeガスの通気性とGM冷凍機の連続運転に対する耐久性とを備えた試料が得られなかったので、HIP焼結での焼結条件を検討した。試料1で作製したGdSの転動造粒粒子をアルミナ製ルツボに充填し、アルゴン雰囲気(150MPa)で、焼成温度を1000℃、焼成時間を3時間とし、HIP焼成を行った。1次粒子の平均結晶粒径は0.1μm、構成粒子の相対密度は56%で、構成粒子の内部では1次粒子と1次粒子との間で僅かにネックが成長している程度であった。この試料を試料1と同様に回転バレル加工したところ、加工中に構成粒子の一部が破壊した。フィルタを通して破壊された試料を除き、試料1と同様にして、1000時間連続で冷凍機を運転したところ、多量の微粉が発生した。
【0033】
HIP焼成の条件を、1200℃でAr圧を200MPa、焼成時間を8時間として、試料1で用いた転動造粒粒子を焼成した。構成粒子の相対密度は67%、1次粒子の平均結晶粒径は0.8μmで、1次粒子間はネックで互いに結合されていた。この試料を試料1と同様に回転バレル加工し、篩い分けと形状分級とを行い、蓄冷材として冷凍機で1000時間及び3000時間連続運転した。回転バレル加工での構成粒子の破壊は見られず、1000時間あるいは3000時間連続運転しても、微粉の発生は生じず、冷凍能力の初期値は試料1と同様であった。
【0034】
HIP焼成の条件を、1300℃でAr圧を60MPa、焼成時間を3時間として、試料1で用いた転動造粒粒子を焼成した。構成粒子の相対密度は73%、1次粒子の平均結晶粒径は1.1μmで、1次粒子間はネックで互いに結合されていた。この試料を試料1と同様に回転バレル加工し、篩い分けと形状分級とを行い、蓄冷材として冷凍機で1000時間連続運転した。回転バレル加工での構成粒子の破壊は見られず、1000時間連続運転で微粉の発生は生じず、冷凍能力の初期値は最低到達温度で2.63K、4.2Kでの冷凍能力で 1.91Wであった。
【0035】
HIP焼成の条件を、1180℃でAr圧を200MPa、焼成時間を8時間として、試料1で用いた転動造粒粒子を焼成した。構成粒子の相対密度は66%、1次粒子の平均結晶粒径は0.7μmで、1次粒子間はネックで互いに結合されていた。この試料を試料1と同様に回転バレル加工し、篩い分けと形状分級とを行い、蓄冷材として冷凍機で1000時間及び3000時間連続運転した。回転バレル加工での構成粒子の破壊は見られず、1000時間連続運転で微粉の発生は生じず、冷凍能力の初期値は試料1と同様であった。しかし3000時間連続運転では、微粉の発生が見られた。
【0036】
HIP焼成の条件を、1330℃でAr圧を100MPa、焼成時間を6時間として、試料1で用いた転動造粒粒子を焼成した。構成粒子の相対密度は78%、1次粒子の平均結晶粒径は2.3μmで、1次粒子間はネックで互いに結合されていた。この試料を試料1と同様に回転バレル加工し、篩い分けと形状分級とを行い、蓄冷材として冷凍機で1000時間連続運転した。回転バレル加工での構成粒子の破壊は見られず、1000時間連続運転で微粉の発生は生じず、冷凍能力の初期値は最低到達温度で2.62K、4.2Kでの冷凍能力で1.90Wであった。
【0037】
試料1で作製したGdSの転動造粒粒子をアルミナ製ルツボに充填し、アルゴン雰囲気(100MPa)で、焼成温度を1500℃、焼成時間を3時間で、HIP焼成を行った。得られた試料を試料1と同じ手法で表面加工と篩い分け及び形状分級を行った。構成粒子の相対密度は89%で、平均結晶粒径は5.3μmであった。試料1と同様の方法で、冷凍能力に関する試験を行ったところ、4.2Kでの冷凍能力の初期値は1.51W、最低到達温度は2.63Kであった。
【0038】
平均粒径が0.6μmの酸化ジスプロシウムを試料1と同様に、硫化・成形を行った。得られた顆粒状の2次粒子を試料1と同一条件で処理し(試料3)、試料1と同様の冷凍機試験を行った。その結果、1000時間及び3000時間連続して冷凍機を運転しても、破壊された構成粒子や微粉は確認できなかった。また冷凍能力に関しては、4.2Kでの冷凍能力が1.75Wで、最低到達温度は2.65Kであった。一方試料3で用いたDySの転動造粒顆粒をアルミナ製ルツボに充填し、常圧アルゴン中で1500℃で焼成した試料(試料4)を、試料1と同様に冷凍機試験を行った。その結果、1000時間連続で冷凍機を運転しても、破壊された構成粒子や微粉は確認できなかったが、冷凍能力の初期値は試料3と比較して85%程度に低下した。尚、希土類元素をGdやDyから、他の希土類元素に変更した場合でも、同じような傾向が見られた。
【0039】
試料1で使用した酸化ガドリニウムGdを転動造粒した後に、試料1と同様に硫化反応を行った。硫化反応後の粒子(顆粒状の2次粒子)を、試料1と同一条件で処理し、試料1と同様の構成粒子を得た。4.2Kにおける冷凍能力及び最低到達温度は試料1と同様であり、連続1000時間及び3000時間冷凍機を運転しても、安定した出力を得ることができた。
【0040】
試料1で使用した酸化ガドリニウムと、酸化テルビウム(平均粒径0.69μm)を混合した以外は、試料1と同様に、硫化・成形・HIP焼結を行なった。このようにして、ガドリニウム−テルビウム系オキシ硫化物(GdTb2−xS、0≦X≦2)の1次粒子がネックで互いに結合された、多孔質の2次粒子からなる多孔質蓄冷材を得た(試料5)。得られた蓄冷材の冷凍能力を、試料1と同様の手法で評価した。結果を表1に示し、冷凍能力は初期値と1000時間連続運転後の2つの値で示す。
【0041】
【表1】

Figure 2004075884
【0042】
表1から明らかなように、xの値を変化させても、無負荷時の最低到達温度及び4.2Kにおける冷凍能力に著しい変化は見られなかった。試料1と同様に連続1000時間冷凍機を運転しても、安定した出力を得ることができた。尚、希土類元素をGd及びTbを他の希土類元素に変更した場合でも、同様の傾向が見られた。実施例ではGdTb2−xSを中心に説明したが、他の希土類オキシ硫化物セラミックス蓄冷材でも同様である。
【図面の簡単な説明】
【図1】実施例のGdSセラミックス蓄冷材での構成粒子の粒子構造を示す、SEM型の電子顕微鏡写真で、下部の水平なバーは5μm長を示す。[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a compound represented by the general formula R 2 O 2 S (R is Y containing La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb and Lu. The present invention relates to a rare earth oxysulfide regenerative material represented by the following formula, and a method for producing the regenerative material, and a regenerator using the regenerative material. More specifically, the present invention relates to a regenerator material which is less likely to be pulverized during operation of a refrigerator, has excellent durability, and has excellent refrigerating capacity in an extremely low temperature region, a method for producing the same, and a regenerator using the same.
[0002]
[Prior art and its problems]
Liquid helium is indispensable for cooling superconducting magnets and sensors, and liquefaction of helium gas requires enormous compression work, which requires a large refrigerator. However, it is difficult to use a large refrigerator for a small device utilizing superconductivity such as a linear motor car or an MRI (magnetic resonance diagnostic device). Therefore, it is essential to develop a compact and high-performance refrigerator capable of generating a liquid helium temperature (4.2 K). Such refrigerators are required to be lightweight and small and have excellent thermal efficiency. For example, in a superconducting MRI apparatus, for example, a GM refrigerator (a small helium refrigerator of the Gifford McMahon type) is used. The GM refrigerator mainly includes a compressor for compressing a working medium such as He gas, an expansion unit for expanding the compressed working medium, and a cryogenic regenerator for maintaining a cooling state of the working medium cooled in the expansion unit. It is configured. Then, at about 60 cycles per minute, the working medium compressed by the compressor is expanded and cooled by the refrigerator, and the system to be cooled is cooled through the distal end of the expansion section of the refrigerator.
[0003]
The cooling capacity and the minimum attainable temperature of the small refrigerator depend on the cold storage material incorporated in the refrigerator, and the cold storage material needs to have a large heat capacity and high heat exchange efficiency. With a conventional metal regenerative material such as Pb, the heat capacity drops sharply at a low temperature of 10K or less. Therefore, a regenerative material for rare earth intermetallic compounds such as HoCu 2 and ErNi having a large heat capacity up to the vicinity of the liquefied helium temperature (4.2 K) has been developed (Japanese Patent No. 2609747). However, the heat storage capacity of the rare earth intermetallic compound regenerator material is significantly reduced below 7K, and the heat capacity in the extremely low temperature region around 4.2K is less than 0.3 J / cc · K. In order to sufficiently maintain the refrigerating capacity in the cryogenic temperature range, the heat capacity of the cold storage material at that temperature is required to be 0.3 J / cc · K or more, and the cold storage material of a rare earth intermetallic compound such as HoCu 2 ErNi is used in the cryogenic temperature range. Refrigeration capacity is insufficient. In addition, rare earth intermetallic compounds are extremely expensive, and cold storage materials using them in the order of several hundred grams are also extremely expensive.
[0004]
The rare earth intermetallic compound cold storage material is prepared by quenching and solidifying a molten metal as disclosed in Japanese Patent No. 2609747 and the like. Naturally, it is a solid, dense granular material having an average particle size of 0.01 to It is about 3 mm. When the average particle size of the granules is increased, the gas flow resistance of the He gas decreases, but the heat exchange efficiency decreases. When the average particle size is reduced, the heat exchange efficiency increases, but the gas flow resistance sharply increases.
[0005]
It has been studied to fix the particles of the rare earth intermetallic compound to each other to increase the strength of the cold storage material and improve the air permeability. For example, Japanese Patent Application Laid-Open No. H11-264618 proposes that a surface of a particle of a rare earth intermetallic compound is coated with a low melting point metal such as Pb, In, or Sn, and the particles are fixed to each other by liquid phase sintering. I have. However, it is difficult to obtain fine particles of the rare earth intermetallic compound, and the average particle diameter of the particles is, for example, 100 to 250 μm. Since the average particle diameter is large, the heat exchange efficiency is limited.
[0006]
[Problems of the Invention]
An object of the present invention is to improve the refrigeration capacity of a refrigerator,
・ It is possible to improve the permeability of high pressure He gas and reduce pressure loss,
Sufficiently withstands vibration and shock due to reciprocating motion of a working medium such as high-pressure He gas during operation of the refrigerator, or hydrodynamic stress due to high-pressure He gas passing inside the regenerator;
It is an object of the present invention to provide a rare earth oxysulfide ceramic regenerator material capable of maintaining excellent refrigerating capacity in a cryogenic region for a long time, a method for producing the same, and a regenerator.
[0007]
Configuration of the Invention
Rare earth oxysulfide ceramic regenerator material of the present invention,
General formula R 2 O 2 S (R is at least one rare earth element selected from La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb and Lu containing Y In a cold storage material using a rare earth oxysulfide represented by
The crystal particles of the rare earth oxysulfide are primary particles, and the primary particles are porous particles sintered together at a neck as constituent particles.
[0008]
Preferably, the average crystal grain size of the crystal grains is 0.2 to 5 μm, more preferably 0.5 to 3 μm, most preferably 0.9 to 2 μm (Claim 2).
[0009]
The relative density of the porous body is preferably 60 to 85%, more preferably 65 to 80%, and most preferably 70 to 75% (Claim 3).
[0010]
The rare earth element constituting the rare earth oxysulfide is optional, but has a specific heat peak temperature of about 4 to 7 K lower than the rare earth intermetallic compound, and is suitable for cooling to liquid helium temperature, such as Gd or Tb, or Dy, Ho, or the like, which has a specific heat peak temperature of about 2 to 4 K and is suitable for cooling to a temperature lower than the liquid helium temperature, is preferable. The rare earth oxysulfide regenerator material need not be one type of constituent rare earth elements, for example, as Gd x Tb 2-x O 2 S, may be used two or more types of constituent rare earth elements. Preferably, at least 80 atomic% of the constituent rare earth elements in the rare earth oxysulfide are Gd, Tb, Dy, or Ho (claim 4).
[0011]
The method for producing a rare earth oxysulfide ceramic regenerator material of the present invention comprises:
General formula R 2 O 2 S (R is at least one rare earth element selected from La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb and Lu containing Y In the method for producing a cold storage material using a rare earth oxysulfide represented by
Granulate the rare earth oxysulfide powder into granules,
The granules are subjected to HIP baking at 1150 to 1350 ° C. to form rare earth oxysulfide crystal particles as primary particles, and the primary particles are used as a cold storage material composed of a porous body sintered together at a neck. (Claim 5).
[0012]
The HIP temperature is more preferably set to 1200 to 1300 ° C.
Preferably, the pressure in the HIP is set to 50 to 200 MPa, and the firing time is set to 1 to 10 hours (claim 6).
[0013]
The cryogenic regenerator according to the present invention uses the rare earth oxysulfide ceramic regenerative material according to any one of claims 1 to 4 (claim 7).
[0014]
Function and Effect of the Invention
In the rare earth oxysulfide ceramic cold storage material of the present invention, a porous body (secondary particle) obtained by sintering primary particles made of crystal particles with each other at a neck is used as constituent particles. In ceramics, the particle size of primary particles can be extremely small, for example, about 0.2 to 5 μm. For this reason, He gas flows inside the porous body and exchanges heat with the primary particles, so that the heat exchange efficiency can be improved. The fine primary particles are sintered together at the neck, making the porous body as a whole a strong material. It is also possible for a plurality of crystal particles to be present in one primary particle, but a plurality of crystal particles closely adhered in the primary particle are fused during the sintering process, and in principle, one crystal particle is formed. Growing into particles.
[0015]
As described above, according to the present invention, a regenerator or a regenerator having high heat exchange efficiency and low pressure loss can be obtained because the constituent particles are porous and the gas permeability of He gas is high. Moreover, since the primary particles are sintered at the neck of each other, the cold storage material and the animal cooler of the present invention have high strength of constituent particles and can withstand vibration, impact, stress, etc. in the refrigerator. Therefore, excellent refrigeration capacity can be maintained for a long time (claims 1 and 7). On the other hand, in the case of metal, it is difficult to obtain fine primary particle powder itself, and even if the primary particles are sintered together to form a porous body, the size of the primary particles is large, so that heat exchange is not possible. It is difficult to improve efficiency.
[0016]
The average crystal grain size of the rare earth oxysulfide ceramic regenerator is preferably 0.2 to 5 μm as an average crystal grain size after HIP firing, because it is involved in improving the permeability of high-pressure He gas and reducing pressure loss. The thickness is more preferably 0.5 to 3 μm, and still more preferably 0.9 to 2 μm. When the average crystal grain size exceeds 5 μm, the heat exchange efficiency between the high-pressure He gas and the primary particles decreases, and when the average crystal grain size is less than 0.2 μm, the permeability of the high-pressure He gas inside the constituent particles is remarkable. And the pressure loss increases. The airflow resistance inside the constituent particles is a viscous resistance, and the viscous resistance is inversely proportional to the size of the void through which the high-pressure He gas flows. The size of the void is proportional to the size of the primary particles.
[0017]
The average crystal grain size of the primary particles is also restricted by the preparation of ceramics. Considering the particle size of the primary particles in the ceramic powder before sintering, it is difficult to make the average crystal particle size of the primary particles in the cold storage material after sintering smaller than this. It is difficult to make the average particle size of the primary particles sufficiently smaller than 0.2 μm from the viewpoint of powder handling properties. Making the average crystal grain size of the primary particles 0.2 μm or more in this way also means that the raw material powder of the ceramic regenerator can be easily obtained (Claim 2).
[0018]
The relative density of the constituent particles in the rare earth oxysulfide ceramic regenerator is preferably from 60 to 85%, more preferably from 65 to 80%, further preferably from 70 to 75%. The strength of the constituent particles depends on the relative density. For example, when the relative density is about 50%, it is difficult to withstand vibration, impact, and stress due to the movement of the high-pressure He gas. The strength of the constituent particles increases exponentially with the relative density when the relative density is in the range of about 50 to 70%. On the other hand, the air permeability in the constituent particles rapidly decreases with the relative density. Particularly, when the relative density exceeds 80%, the air permeability decreases exponentially with the density, and when the relative density exceeds 85%, the air permeability extremely decreases. Therefore, when the relative density of the constituent particles is set to 60 to 85%, the strength of the constituent particles can be secured, and the air permeability in the constituent particles can be secured (claim 3).
[0019]
When the constituent rare earth elements in the rare earth oxysulfide ceramics are Gd and Tb, a specific heat peak appears at about 4 to 7 K, which is lower than the specific heat peak of the rare earth intermetallic compound, and is necessary for cooling to the liquid He temperature. Are suitable. Note that the specific heat peak (magnetic phase transition temperature) of Gd 2 O 2 S is 5.2K, that of Tb 2 O 2 S is 6.3K, and that Gd x Tb 2-x O 2 S (0 ≦ X ≦ 1.8) In this case, a peak of specific heat appears at about 4.2 to 5.3K. Further, when the rare earth intermetallic compound cold storage material is arranged on the high temperature side of the rare earth oxysulfide ceramic cold storage material, it can be efficiently cooled to the liquid He temperature. When the constituent rare earth element of the rare earth oxysulfide ceramic regenerator material and Dy and Ho, the peak of the specific heat at Dy 2 O 2 S becomes 2.2K at 4.6K, Ho 2 O 2 S. Thus Gd 2 O 2 S and Tb 2 O 2 S, Gd x Tb 2-x O 2 S a (0 <X <2) disposed on the high temperature side, Dy 2 O 2 S and Ho 2 O in the cold side When placing the 2 S, cooling is facilitated to a lower temperature (claim 4).
[0020]
To produce the rare earth oxysulfide cold accumulating material of the present invention, for example, raw materials of rare earth oxide powder, H 2 S under heating by flowing a gas containing an oxidizing number -2 sulfur atoms, such as CH 3 SH reaction Thus, a rare earth oxysulfide powder is produced, and this powder is granulated. Alternatively, the rare earth oxide powder may be granulated and then reacted with a gas containing a sulfur atom having an oxidation number of -2 to form a rare earth oxysulfide. The method of granulation itself is arbitrary, and may be, for example, tumbling granulation, a combination of extrusion and tumbling granulation, fluidized granulation, spray drying granulation, embossing granulation, and the like.
[0021]
In order to obtain a rare earth oxysulfide ceramic regenerator material, it is preferable to fire the granulated particles by HIP (hot isostatic pressure). In the conventional normal pressure firing method, when high-temperature firing is performed, a neck between primary particles grows. At the same time, however, grain growth and densification occur. I can not secure it. On the other hand, when low-temperature firing is performed to suppress grain growth and densification, necks between primary particles do not grow, and the strength of constituent particles cannot be obtained. An inert gas such as argon is used as a firing atmosphere (pressure medium) of the HIP, a firing temperature is 1150 to 1350 ° C., particularly 1200 to 1300 ° C., and a firing time is a holding time to a peak temperature of 1 to 10 hours. Is preferably 50 to 200 MPa. These are experimentally obtained under the conditions that the relative density of the constituent particles is 60 to 85%.
[0022]
The diameter of the sphere (circumscribed sphere) containing the constituent particles affects the air permeability, the heat exchange efficiency, and the strength, and the average diameter is preferably 0.01 to 2 mm. The aspect ratio (the ratio of the major axis to the minor axis) of the constituent particles is preferably 3 or less, more preferably 2 or less, and particularly preferably 1.2 or less. This is because, as the aspect ratio is smaller, uniform filling is easier, and the generation of fine powder due to vibration, impact, and stress due to the movement of the high-pressure He gas is smaller. However, the aspect ratio of the primary particles themselves is arbitrary, and it is preferable that non-spherical primary particles be bonded to each other inside the constituent particles to obtain a large void.
[0023]
The regenerator of the present invention is a regenerator having the above-described rare earth oxysulfide ceramic regenerator filled in a regenerator cylinder. For example, the regenerator may be divided into a plurality of layers and each layer may be filled with another regenerator. Further, it is preferable that the high-temperature side of the rare-earth oxysulfide ceramic regenerator is filled with a rare-earth intermetallic regenerative material such as HoCu 2 so that the specific heat is continuous from the high-temperature side to the lowest temperature.
[0024]
【Example】
Examples will be described below.
[0025]
[Sample 1]
The average particle diameter of gadolinium oxide Gd 2 O 3 was 0.46 μm according to the Fisher method. This gadolinium oxide is filled in a quartz boat and reacted at 650 ° C. while flowing hydrogen sulfide gas H 2 S through a quartz reaction tube. When the X-ray diffraction of the reaction product was measured, only a peak of gadolinium oxysulfide Gd 2 O 2 S alone was recognized, and the reaction yield with respect to the rare earth oxide was 100%. The obtained Gd 2 O 2 S powder (average particle size 0.46 μm) was tumbled and granulated. The tumbled and granulated powder was filled in an alumina crucible, and the furnace was sufficiently evacuated to perform HIP firing. After that, the inside of the furnace was sufficiently evacuated, and argon gas was introduced and firing was performed in an argon atmosphere. By setting the firing temperature to 1250 ° C., the pressure to 150 MPa, and the firing time to 5 hours, constituent particles having a relative density of 72% of the theoretical density by a pycnometer method were obtained.
[0026]
The fired constituent particles, nylon-based media, and 10 wt% alumina slurry were charged into a processing tank, and surface processing was performed by a rotary barrel processing method. When the processing time was set to 2 hours, crystal particles existing as protrusions on the surface of the constituent particles could be removed. The observation of the surface state was performed by a scanning electron microscope (SEM). The surface-processed constituent particles are sieved with a filter net, and the sieved constituent particles are rolled on an iron plate (polished to a mirror surface) inclined at about 25 °, and the rolling-down constituent particles are collected and classified. Was performed. For 100 constituent particles, the average diameter of the spheres containing the constituent particles was 0.4 mm, and the average aspect ratio of the constituent particles was 1.1. The average particle diameter and the average aspect ratio of the constituent particles were measured from images taken using a video high scope system. The constituent particles after shape classification are referred to as Sample 1.
[0027]
The constituent particles were fixed in plastic, cut, and the primary particles inside were observed by SEM. An SEM photograph is shown in FIG. Observation with an SEM revealed that the average particle size of the crystal particles constituting the constituent particles was 1.1 μm. The relative density was 72% as described above. The crystal grains were sintered and fixed to each other at the neck, and voids were left between the crystal grains, and the voids communicated to form open pores. Further, the constituent particles did not adhere to each other.
[0028]
Next, in order to examine the strength of the constituent particles, 100 constituent particles were put into a rectangular plastic bag having a side of 5 cm and the other side of 10 cm, and shaken for 120 minutes / minute with a shaker for 5 minutes. Inspection of the crushed state of the sample showed no destruction of constituent particles or generation of fine powder.
[0029]
After the thus obtained constituent particles are filled in the cooling section of the GM refrigerator in a close-packed manner, He gas having a heat capacity of 25 J / K is supplied at a mass flow rate of 3 g / sec and a gas pressure of 16 atm under the GM conditions. The refrigeration cycle was continued for 1000 hours and 3000 hours. The constituent particles after 1000 hours and 3000 operation were observed, but no broken constituent particles or fine powder were observed. The refrigeration characteristics of the above constituent particles were examined using a two-stage GM refrigerator with a power consumption of 3.4 kW. Pb was used for the first-stage regenerator on the high-temperature side, and 50 vol% of HoCu 2 was placed on the high-temperature side of the second-stage regenerator, and 50 vol% of constituent particles of sample 1 was placed on the low-temperature side of the second-stage regenerator. After loading, the refrigeration capacity was checked. The refrigerating capacity at 4.2 K was 1.94 W, and the minimum temperature at the time of no load was 2.62 K. Even if the refrigerator was operated continuously for 1000 hours or 3000 hours, there was no change in the refrigerating capacity or the minimum attained temperature.
[0030]
The sintering method and the sintering conditions were changed for the granulated by rolling in Sample 1, and the strength and refrigerating characteristics of the regenerator material were evaluated. The rolled granules of Gd 2 O 2 S used in Sample 1 were filled in an alumina crucible and fired at a firing temperature of 1250 ° C. for 5 hours in an argon atmosphere at normal pressure. When this sample was subjected to rotary barrel processing in the same manner as Sample 1, a large amount of fine powder was generated during the processing, so that no further test was carried out because it was not usable as a cold storage material (Sample 2). In the SEM, the neck was slightly growing between the primary particles and the relative density of the secondary particles (sintered individual granules) by the pycnometer method was 52%. .
[0031]
Since the sintering temperature of Sample 2 was too low, the sintering temperature was changed to 1350 ° C and 1500 ° C by normal pressure sintering. At 1350 ° C., the secondary particles were porous, but the formation of necks between the primary particles was slight, and a large amount of fine powder was generated by rotating barrel processing. After sintering at 1500 ° C., the relative density of the secondary particles was 99.9%, and the average crystal grain size was 3.2 μm. This sample was subjected to surface processing, sieving, and shape classification in the same manner as Sample 1, and charged into a refrigerator as a regenerator material, and the refrigerator was operated continuously for 1000 hours. The refrigerating capacity at 4.2 K was 1.69 W, the minimum temperature reached 2.62 K, and the refrigerating capacity was reduced to 85% as compared with Sample 1.
[0032]
In the normal pressure sintering, a sample having sufficient permeability of He gas and durability with respect to continuous operation of the GM refrigerator was not obtained because the sample was porous and the primary particles were bonded by a neck. The sintering conditions in sintering were studied. The rolled granulated particles of Gd 2 O 2 S prepared in Sample 1 were filled in an alumina crucible, and HIP firing was performed in an argon atmosphere (150 MPa) at a firing temperature of 1000 ° C. and a firing time of 3 hours. The average crystal grain size of the primary particles is 0.1 μm, the relative density of the constituent particles is 56%, and the neck is slightly growing between the primary particles within the constituent particles. Was. When this sample was subjected to rotary barrel processing in the same manner as Sample 1, some of the constituent particles were broken during the processing. Except for the sample destroyed through the filter, the refrigerator was operated continuously for 1000 hours in the same manner as in Sample 1, and a large amount of fine powder was generated.
[0033]
The rolling granulated particles used in Sample 1 were fired under the conditions of HIP firing at 1200 ° C., an Ar pressure of 200 MPa, and a firing time of 8 hours. The relative density of the constituent particles was 67%, the average crystal grain size of the primary particles was 0.8 μm, and the primary particles were connected to each other by a neck. This sample was subjected to rotary barrel processing in the same manner as Sample 1, subjected to sieving and shape classification, and was continuously operated as a cold storage material by a refrigerator for 1000 hours and 3000 hours. No destruction of the constituent particles was observed in the rotary barrel processing, and no fine powder was generated even after continuous operation for 1000 hours or 3000 hours, and the initial value of the refrigerating capacity was similar to that of Sample 1.
[0034]
The rolling granules used in Sample 1 were fired under the conditions of HIP firing at 1300 ° C., an Ar pressure of 60 MPa and a firing time of 3 hours. The relative density of the constituent particles was 73%, and the average crystal grain size of the primary particles was 1.1 μm. The primary particles were connected to each other by a neck. This sample was subjected to rotary barrel processing in the same manner as Sample 1, subjected to sieving and shape classification, and was continuously operated as a cold storage material by a refrigerator for 1000 hours. No destruction of the constituent particles was observed in the rotary barrel processing, no fine powder was generated during continuous operation for 1000 hours, and the initial value of the refrigerating capacity was 2.63K at the lowest temperature and 4.2F at 4.2K. It was 91W.
[0035]
The rolling granules used in Sample 1 were fired under the conditions of HIP firing at 1180 ° C., an Ar pressure of 200 MPa, and a firing time of 8 hours. The relative density of the constituent particles was 66%, the average crystal grain size of the primary particles was 0.7 μm, and the primary particles were connected to each other by a neck. This sample was subjected to rotary barrel processing in the same manner as Sample 1, subjected to sieving and shape classification, and was continuously operated as a cold storage material by a refrigerator for 1000 hours and 3000 hours. No destruction of the constituent particles was observed in the rotating barrel processing, no fine powder was generated during continuous operation for 1000 hours, and the initial value of the refrigerating capacity was similar to that of Sample 1. However, in the continuous operation for 3000 hours, generation of fine powder was observed.
[0036]
The rolling granules used in Sample 1 were fired under the conditions of HIP firing at 1330 ° C., an Ar pressure of 100 MPa, and a firing time of 6 hours. The relative density of the constituent particles was 78%, the average crystal grain size of the primary particles was 2.3 μm, and the primary particles were connected to each other by a neck. This sample was subjected to rotary barrel processing in the same manner as Sample 1, subjected to sieving and shape classification, and was continuously operated as a cold storage material by a refrigerator for 1000 hours. No destruction of the constituent particles was observed in the rotary barrel processing, no fine powder was generated during continuous operation for 1000 hours, and the initial value of the refrigerating capacity was 1.62 K at the lowest attained temperature and 1. at the refrigerating capacity at 4.2 K. It was 90W.
[0037]
The rolled granulated particles of Gd 2 O 2 S prepared in Sample 1 were filled in an alumina crucible, and HIP firing was performed in an argon atmosphere (100 MPa) at a firing temperature of 1500 ° C. and a firing time of 3 hours. The obtained sample was subjected to surface processing, sieving and shape classification in the same manner as Sample 1. The relative density of the constituting particles was 89%, and the average crystal grain size was 5.3 μm. When a test on the refrigerating capacity was performed in the same manner as in Sample 1, the initial value of the refrigerating capacity at 4.2 K was 1.51 W, and the lowest temperature was 2.63 K.
[0038]
Dysprosium oxide having an average particle size of 0.6 μm was sulfurized and molded in the same manner as in Sample 1. The obtained granular secondary particles were treated under the same conditions as Sample 1 (Sample 3), and a refrigerator test similar to that of Sample 1 was performed. As a result, even if the refrigerator was operated continuously for 1000 hours and 3000 hours, no broken constituent particles or fine powder could be confirmed. As for the refrigerating capacity, the refrigerating capacity at 4.2 K was 1.75 W, and the minimum temperature was 2.65 K. On the other hand, the rolling granules of Dy 2 O 2 S used in Sample 3 were filled in an alumina crucible, and fired at 1500 ° C. in argon under normal pressure (Sample 4). Was done. As a result, even if the refrigerator was operated continuously for 1000 hours, no broken constituent particles or fine powder could be confirmed, but the initial value of the refrigerating capacity was reduced to about 85% as compared with Sample 3. A similar tendency was observed when the rare earth element was changed from Gd or Dy to another rare earth element.
[0039]
After subjecting the gadolinium oxide Gd 2 O 3 used in Sample 1 to tumbling granulation, a sulfidation reaction was performed in the same manner as in Sample 1. The particles after the sulfidation reaction (granular secondary particles) were treated under the same conditions as in Sample 1 to obtain the same constituent particles as Sample 1. The refrigerating capacity and the lowest temperature reached at 4.2 K were the same as those of Sample 1, and a stable output could be obtained even when the refrigerator was operated continuously for 1000 hours and 3000 hours.
[0040]
Sulfidation, molding, and HIP sintering were performed in the same manner as in Sample 1, except that gadolinium oxide used in Sample 1 and terbium oxide (average particle size: 0.69 μm) were mixed. In this way, the porous particles composed of the porous secondary particles in which the primary particles of gadolinium-terbium-based oxysulfide (Gd x Tb 2-x O 2 S, 0 ≦ X ≦ 2) are bonded to each other at the neck. A cold storage material was obtained (Sample 5). The refrigerating capacity of the obtained regenerator material was evaluated in the same manner as in Sample 1. The results are shown in Table 1, and the refrigerating capacity is shown by an initial value and two values after continuous operation for 1000 hours.
[0041]
[Table 1]
Figure 2004075884
[0042]
As is clear from Table 1, even when the value of x was changed, no remarkable change was observed in the minimum attained temperature at no load and the refrigerating capacity at 4.2K. Even when the refrigerator was operated continuously for 1000 hours in the same manner as in Sample 1, a stable output was obtained. Note that the same tendency was observed when the rare earth element was changed from Gd and Tb to another rare earth element. In the embodiment, Gd x Tb 2-x O 2 S has been mainly described, but the same applies to other rare earth oxysulfide ceramic regenerator materials.
[Brief description of the drawings]
FIG. 1 is an SEM-type electron micrograph showing the particle structure of constituent particles of a Gd 2 O 2 S ceramic regenerator according to an example. The lower horizontal bar shows a length of 5 μm.

Claims (7)

一般式 RS (RはYを含むLa, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb及びLuから選択される少なくとも1種類の希土類元素を表す。)で表される希土類オキシ硫化物を用いた蓄冷材において、
前記希土類オキシ硫化物の結晶粒子を1次粒子とし、該1次粒子がネックで互いに焼結された多孔質体を構成粒子とすることを特徴とする、希土類オキシ硫化物セラミックス蓄冷材。
General formula R 2 O 2 S (R is at least one rare earth element selected from La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb and Lu containing Y In a cold storage material using a rare earth oxysulfide represented by:
A rare earth oxysulfide ceramic regenerator material, wherein the rare earth oxysulfide crystal particles are primary particles, and the primary particles are porous particles sintered together at a neck.
前記結晶粒子の平均結晶粒径が0.2〜5μmであることを特徴とする、請求項1の希土類オキシ硫化物セラミックス蓄冷材。The rare earth oxysulfide ceramic cold storage material according to claim 1, wherein the average crystal grain size of the crystal grains is 0.2 to 5 µm. 前記多孔質体は相対密度が60〜85%であることを特徴とする、請求項1または2の希土類オキシ硫化物セラミックス蓄冷材。The rare earth oxysulfide ceramic cold storage material according to claim 1 or 2, wherein the porous body has a relative density of 60 to 85%. 前記希土類オキシ硫化物の構成希土類元素の80原子%以上が、Gd,Tb,Dy,またはHoであることを特徴とする、請求項1〜3のいずれかの希土類オキシ硫化物セラミックス蓄冷材。The rare earth oxysulfide ceramic regenerator according to any one of claims 1 to 3, wherein 80% by atom or more of the rare earth element constituting the rare earth oxysulfide is Gd, Tb, Dy, or Ho. 一般式 RS (Rは Yを含むLa, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb及びLuから選択される少なくとも1種類の希土類元素を表す。) で表される希土類オキシ硫化物を用いた蓄冷材の製造方法において、
前記希土類オキシ硫化物の粉体を顆粒に造粒し、
該顆粒を1150〜1350℃でHIP焼成して、希土類オキシ硫化物の結晶粒子を1次粒子とし、該1次粒子がネックで互いに焼結された多孔質体からなる蓄冷材とすることを特徴とする、希土類オキシ硫化物セラミックス蓄冷材の製造方法。
General formula R 2 O 2 S (R is at least one rare earth element selected from La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb and Lu containing Y In the method for producing a cold storage material using a rare earth oxysulfide represented by
Granulate the rare earth oxysulfide powder into granules,
The granules are subjected to HIP baking at 1150 to 1350 ° C. to form rare earth oxysulfide crystal particles as primary particles, and the primary particles are used as a cold storage material composed of a porous body sintered together at a neck. A method for producing a rare earth oxysulfide ceramic cold storage material.
前記HIPでの圧力が50〜200MPa,焼成時間が1〜10時間であることを特徴とする、請求項5の希土類オキシ硫化物セラミックス蓄冷材の製造方法。The method for producing a cold storage material for rare earth oxysulfide ceramics according to claim 5, wherein the pressure at the HIP is 50 to 200 MPa and the sintering time is 1 to 10 hours. 請求項1〜4のいずれかの希土類オキシ硫化物セラミックス蓄冷材を用いた、極低温蓄冷器。A cryogenic regenerator using the rare earth oxysulfide ceramic regenerative material according to claim 1.
JP2002239192A 2002-08-20 2002-08-20 Rare earth oxysulfide ceramic regenerator material and method for producing the same, and cryogenic regenerator using the regenerator material Expired - Fee Related JP4170703B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002239192A JP4170703B2 (en) 2002-08-20 2002-08-20 Rare earth oxysulfide ceramic regenerator material and method for producing the same, and cryogenic regenerator using the regenerator material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002239192A JP4170703B2 (en) 2002-08-20 2002-08-20 Rare earth oxysulfide ceramic regenerator material and method for producing the same, and cryogenic regenerator using the regenerator material

Publications (2)

Publication Number Publication Date
JP2004075884A true JP2004075884A (en) 2004-03-11
JP4170703B2 JP4170703B2 (en) 2008-10-22

Family

ID=32022360

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002239192A Expired - Fee Related JP4170703B2 (en) 2002-08-20 2002-08-20 Rare earth oxysulfide ceramic regenerator material and method for producing the same, and cryogenic regenerator using the regenerator material

Country Status (1)

Country Link
JP (1) JP4170703B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004123884A (en) * 2002-10-02 2004-04-22 Konoshima Chemical Co Ltd Rare earth oxysulfide ceramic regenerator material, method for producing the same, and cryogenic regenerator using the regenerator material
JP2004189906A (en) * 2002-12-12 2004-07-08 Toshiba Corp Cold storage material, method for producing the same, and cold storage refrigerator
WO2016047419A1 (en) * 2014-09-25 2016-03-31 株式会社東芝 Rare-earth cold storage material particles, refrigerator using same, superconducting magnet, inspection device, and cryopump
WO2018117258A1 (en) * 2016-12-22 2018-06-28 株式会社三徳 Cooling storage material and method for producing same, cooling storage device, and refrigerating machine
JP2018173268A (en) * 2012-10-09 2018-11-08 株式会社東芝 Cold head manufacturing method

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004123884A (en) * 2002-10-02 2004-04-22 Konoshima Chemical Co Ltd Rare earth oxysulfide ceramic regenerator material, method for producing the same, and cryogenic regenerator using the regenerator material
JP2004189906A (en) * 2002-12-12 2004-07-08 Toshiba Corp Cold storage material, method for producing the same, and cold storage refrigerator
JP2018173268A (en) * 2012-10-09 2018-11-08 株式会社東芝 Cold head manufacturing method
US11692117B2 (en) 2012-10-09 2023-07-04 Kabushiki Kaisha Toshiba Rare earth regenerator material particle, rare earth regenerator material particle group, and cold head, superconducting magnet, examination apparatus, and cryopump using the same
US11015101B2 (en) 2012-10-09 2021-05-25 Kabushiki Kaisha Toshiba Rare earth regenerator material particle, rare earth regenerator material particle group, and cold head, superconducting magnet, examination apparatus, and cryopump using the same
US10513646B2 (en) 2012-10-09 2019-12-24 Kabushiki Kaisha Toshiba Rare earth regenerator material particle, rare earth regenerator material particle group, and cold head, superconducting magnet, examination apparatus, and cryopump using the same
US11059725B2 (en) 2014-09-25 2021-07-13 Kabushiki Kaisha Toshiba Rare earth cold accumulating material particles, and refrigerator, superconducting magnet, inspection device and cryopump using same
CN112251199A (en) * 2014-09-25 2021-01-22 株式会社东芝 Rare earth cold storage material particles, and refrigerator, superconducting magnet, inspection device, and cryopump using the same
US10155668B2 (en) 2014-09-25 2018-12-18 Kabushiki Kaisha Toshiba Rare earth cold accumulating material particles, and refrigerator, superconducting magnet, inspection device and cryopump using same
WO2016047419A1 (en) * 2014-09-25 2016-03-31 株式会社東芝 Rare-earth cold storage material particles, refrigerator using same, superconducting magnet, inspection device, and cryopump
JP2020023713A (en) * 2014-09-25 2020-02-13 株式会社東芝 Rare-earth cold storage material particle, refrigerator with the same, superconductive magnet, testing equipment, and cryopump
JP2020029397A (en) * 2014-09-25 2020-02-27 株式会社東芝 Rare-earth regenerator particles, refrigerator using the same, superconducting magnet, inspection device, and cryopump
CN112251200A (en) * 2014-09-25 2021-01-22 株式会社东芝 Rare earth cold storage material particles, and refrigerator, superconducting magnet, inspection device, and cryopump using the same
US11649171B2 (en) 2014-09-25 2023-05-16 Kabushiki Kaisha Toshiba Refrigerator including rare earth cold accumulating material particles, and superconducting magnet, inspection device and cryopump using same
JPWO2016047419A1 (en) * 2014-09-25 2017-07-13 株式会社東芝 Rare earth regenerator particles, refrigerators using them, superconducting magnets, inspection devices and cryopumps
CN106715637A (en) * 2014-09-25 2017-05-24 株式会社东芝 Rare earth cold storage material particles, refrigerators using the particles, superconducting magnets, inspection devices, and cryopumps
JP2021120345A (en) * 2014-09-25 2021-08-19 株式会社東芝 Cryogenic refrigerator, superconducting magnet, mri apparatus, nmr apparatus and cryopump
US11136244B2 (en) 2014-09-25 2021-10-05 Kabushiki Kaisha Toshiba Rare earth cold accumulating material particles, and refrigerator, superconducting magnet, inspection device and cryopump using same
EP3916068A1 (en) 2014-09-25 2021-12-01 Kabushiki Kaisha Toshiba Refrigerator comprising rare earth cold accumulating material particles
JP7055918B2 (en) 2014-09-25 2022-04-18 株式会社東芝 Ultra-low temperature refrigerators, superconducting magnets, MRI equipment, NMR equipment and cryopumps
JP6382470B1 (en) * 2016-12-22 2018-08-29 株式会社三徳 Cold storage material and manufacturing method thereof, cold storage and refrigerator
WO2018117258A1 (en) * 2016-12-22 2018-06-28 株式会社三徳 Cooling storage material and method for producing same, cooling storage device, and refrigerating machine

Also Published As

Publication number Publication date
JP4170703B2 (en) 2008-10-22

Similar Documents

Publication Publication Date Title
US6467277B2 (en) Cold accumulating material, method of manufacturing the same and refrigerator using the material
KR100859347B1 (en) Rare earth oxysulfide accumulators and coolers
JP5455536B2 (en) Refrigerator using cryogenic regenerator material
EP1016701B1 (en) Cold accumulating material and cold accumulation refrigerator using the same
CN109312215B (en) Rare earth sulfur oxide cold storage material
JP3642486B2 (en) Rare earth oxysulfide regenerator and regenerator
JP4030091B2 (en) Rare earth oxysulfide regenerator and regenerator
WO2023032867A1 (en) Granular particles for cold storage material particles, cold storage material particles, cold storage device, refrigerating machine, cryopump, superconducting magnet, nuclear magnetic resonance imaging apparatus, nuclear magnetic resonance apparatus, magnetic field application-type single crystal pulling apparatus, and helium re-condensation apparatus
KR19990087114A (en) Cryogenic coolant and freezer using the same
JP5468380B2 (en) Cold storage material and manufacturing method thereof
JP4170703B2 (en) Rare earth oxysulfide ceramic regenerator material and method for producing the same, and cryogenic regenerator using the regenerator material
JP4170654B2 (en) Rare earth oxysulfide ceramic regenerator material and method for producing the same, and cryogenic regenerator using the regenerator material
JP2002249763A (en) Cold storage material, method for producing the same, and refrigerator using the cold storage material
JPH06240241A (en) Cold-reserving agent for cryogenic temperature and cold-reserving apparatus for cryogenic temperature using the same
JP4564161B2 (en) refrigerator
JP4259837B2 (en) Method for producing rare earth oxysulfide ceramic regenerator material
JP3990894B2 (en) Oxide ceramics regenerator material and its manufacturing method
JP4256664B2 (en) Method for producing rare earth vanadium oxide ceramics
JP3561023B2 (en) Cryogenic cool storage material and cryogenic cool storage device using the same
JP4666570B2 (en) Hybrid regenerator material, its manufacturing method and regenerator
JP2004189906A (en) Cold storage material, method for producing the same, and cold storage refrigerator
JP2004099822A (en) Cool storage material and cool storage refrigerator using the same
RU2834049C2 (en) Granular particle used for refrigerating chamber material particle, refrigerating chamber material particle, refrigerating chamber device, refrigerator, cryogenic vacuum pump, superconducting magnet, nuclear magnetic resonance imaging apparatus, nuclear magnetic resonance apparatus, installation for drawing monocrystals with application of magnetic field and helium recondensation device
JPH031050A (en) Cold heat storage apparatus
JP2006008999A (en) Cryogenic storage material manufacturing method and cryogenic regenerator manufacturing method

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040916

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20080805

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20080807

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110815

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110815

Year of fee payment: 3

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110815

Year of fee payment: 3

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110815

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120815

Year of fee payment: 4

LAPS Cancellation because of no payment of annual fees