JPH0617489B2 - Method and apparatus for manufacturing high-density sintered body - Google Patents
Method and apparatus for manufacturing high-density sintered bodyInfo
- Publication number
- JPH0617489B2 JPH0617489B2 JP60109580A JP10958085A JPH0617489B2 JP H0617489 B2 JPH0617489 B2 JP H0617489B2 JP 60109580 A JP60109580 A JP 60109580A JP 10958085 A JP10958085 A JP 10958085A JP H0617489 B2 JPH0617489 B2 JP H0617489B2
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- gas
- capsule
- sintered body
- density sintered
- 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
Links
- 238000000034 method Methods 0.000 title claims description 31
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 239000007789 gas Substances 0.000 claims description 93
- 239000002775 capsule Substances 0.000 claims description 86
- 239000000463 material Substances 0.000 claims description 28
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 18
- 238000005485 electric heating Methods 0.000 claims description 17
- 229930195733 hydrocarbon Natural products 0.000 claims description 9
- 150000002430 hydrocarbons Chemical class 0.000 claims description 9
- 239000004215 Carbon black (E152) Substances 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 6
- 238000001514 detection method Methods 0.000 claims description 5
- 238000001513 hot isostatic pressing Methods 0.000 claims description 3
- 238000000462 isostatic pressing Methods 0.000 claims 1
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 15
- 238000010438 heat treatment Methods 0.000 description 14
- 229910052799 carbon Inorganic materials 0.000 description 12
- 239000001257 hydrogen Substances 0.000 description 11
- 229910052739 hydrogen Inorganic materials 0.000 description 11
- 239000011230 binding agent Substances 0.000 description 10
- 229910052786 argon Inorganic materials 0.000 description 8
- 239000003575 carbonaceous material Substances 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- 230000006378 damage Effects 0.000 description 5
- 238000000354 decomposition reaction Methods 0.000 description 5
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000011368 organic material Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 229920000049 Carbon (fiber) Polymers 0.000 description 3
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 3
- 230000005856 abnormality Effects 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 3
- 239000004917 carbon fiber Substances 0.000 description 3
- 238000010000 carbonizing Methods 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 3
- 239000011294 coal tar pitch Substances 0.000 description 3
- 239000000571 coke Substances 0.000 description 3
- 230000006835 compression Effects 0.000 description 3
- 238000010304 firing Methods 0.000 description 3
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 239000002006 petroleum coke Substances 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000011269 tar Substances 0.000 description 3
- 239000011271 tar pitch Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- MWPLVEDNUUSJAV-UHFFFAOYSA-N anthracene Chemical compound C1=CC=CC2=CC3=CC=CC=C3C=C21 MWPLVEDNUUSJAV-UHFFFAOYSA-N 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- 239000011295 pitch Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 235000008754 Agave americana Nutrition 0.000 description 1
- 240000004246 Agave americana Species 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- 239000012620 biological material Substances 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 239000011304 carbon pitch Substances 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- -1 for example Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B11/00—Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses
- B30B11/001—Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses using a flexible element, e.g. diaphragm, urged by fluid pressure; Isostatic presses
- B30B11/002—Isostatic press chambers; Press stands therefor
Landscapes
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Powder Metallurgy (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は高密度の炭素材料を工業的製造等において適用
される熱間静水プレス(以下、HIPと略記する)手段
の安全な運転方法ならびに安全装置に係るものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a safe operation method of hot isostatic pressing (hereinafter abbreviated as HIP) means applied to industrial production of high density carbon materials, and It relates to a safety device.
(従来の技術) 炭素材料(ダイヤモンドを除く)は無定形炭素と黒鉛に
二分されるが、各々成形体,繊維など種々の形態のもの
があり、その優れた耐熱成,化学薬品に対する安全成、
特異な電気的性質のため、近年その利用分野はロケット
ノズルなど宇宙材料から心臓の人工弁まで多岐にわたっ
ており、益々その適用分野は広がる傾向にある。(Prior art) Carbon materials (excluding diamond) are divided into amorphous carbon and graphite. There are various forms such as molded bodies and fibers, and their excellent heat resistance, safety against chemicals,
Due to their unique electrical properties, their fields of use have recently been widespread, from space materials such as rocket nozzles to artificial valves of the heart, and their application fields tend to expand.
とくに近年、従来の黒鉛等と異なり高密度または高弾性
の炭素繊維が開発されるに及び構造部材としての用途の
増大は急激である。Particularly, in recent years, unlike conventional graphite and the like, carbon fibers having high density or high elasticity have been developed, and the use as structural members has been rapidly increasing.
しかしながら、これらの機能的な構造材料として使用さ
れる部材は一般に高密度のものが要求され、とりわけ高
密度で、等方的で、かつ大形のものの開発が急がれてい
る。例えば、高密度化することにより材料の強度や、耐
食成が飛躍的に改善され、高温下で使用される化学機器
や生体用材料等の用途への利用が拡大が期待される。ま
た、この数年、需要が増大している放電加工用電極では
切り出し方向により電気特性が異なると電極としての性
能を影響するため等方的であることが求められている。However, members used as these functional structural materials are generally required to have high density, and particularly high density, isotropic and large size members are urgently developed. For example, by increasing the density, the strength and corrosion resistance of the material are dramatically improved, and it is expected that the use thereof will be expanded to applications such as chemical equipment and biomaterials used at high temperatures. Further, in the electric discharge machining electrode, which has been in increasing demand for several years, if the electrical characteristics are different depending on the cutting direction, the performance as the electrode is affected, and therefore it is required to be isotropic.
ところで、従来、これらの炭素材料はコークスなどフィ
ラー材と、タール・ピッチなどのバインダーとを捏合,
成形した後、加熱してバインダーを炭化させるという工
程で製造されるため、バインダーの分解ガスが抜けた気
孔を不可避的に含んでいた。そこで、この気孔の量を減
少させ、高密度化するため、タール・ピッチを含浸し、
これを炭化する操作を繰り返し行うことが行われてい
る。By the way, heretofore, these carbon materials have been obtained by kneading a filler material such as coke and a binder such as tar / pitch,
Since it is manufactured in a step of heating and carbonizing the binder after molding, it inevitably contains pores from which the decomposed gas of the binder has escaped. Therefore, in order to reduce the amount of these pores and increase the density, impregnation with tar pitch,
The operation of carbonizing this is repeatedly performed.
しかしながら、このような工程では焼成時のバインダー
分解を低速で行わないと製品に割れを生じ、かつ炭素の
収率が低いため繰返し数が多くなり、結果として製品の
完成に数ケ月を要するなどの問題が派生している。However, in such a process, if the binder is not decomposed at a low speed during firing, the product will crack, and the carbon yield will be low, resulting in a large number of repetitions. As a result, it will take several months to complete the product. The problem is derived.
また、等方性を得るためには、微粒のコークスを冷間清
水圧成形法(ラバープレス法)で成形するという手段が
採られているが、バインダーの量を20%以上混合しな
いと成形性が悪く、このため最初の焼成後の気孔率を低
減することが困難となっていた。Further, in order to obtain the isotropic property, a means of forming fine coke by a cold fresh water pressure forming method (rubber press method) is adopted, but if the amount of the binder is not mixed with 20% or more, the formability is improved. However, it was difficult to reduce the porosity after the first firing.
このような状況において、上記の各問題を解消する方法
として、分解生成するガス成分のうち、水素のみを透過
するパラジウムなどの缶体に成形体を収納し、缶体外部
からほぼ等方的に圧縮しつつ炭化を行う方法(米国特許
第3,249,964号明細書参照)や、HIP法を利用した特
開昭51−8503号の方法あるいはその発明の有する
欠点を改善した特願昭59−46076号記載の製造方
法ならびに装置が提案されている。In such a situation, as a method for solving each of the above problems, among the gas components decomposed and produced, the molded body is housed in a can body such as palladium that permeates only hydrogen and isotropically isotropic from the outside of the can body. A method of carbonizing while compressing (see US Pat. No. 3,249,964), a method of JP-A-51-8503 utilizing the HIP method, or Japanese Patent Application No. 59-46076 in which the drawbacks of the invention are improved. Have been proposed.
上記HIP法は、焼結性材料をカプセルと呼ばれる気密
の容器内に封入して高圧容器内に挿入し、高圧容器内に
内臓した電熱体により焼結性材料を加熱しつつ高圧容器
内の圧力媒体、例えば、圧媒ガスの等方的な圧縮力によ
る加圧する、所謂、HIPを施すに際し、前記カプセル
内と連通し、高圧容器外へその端部が延長する調整管路
を設け、該調整管路を通じてカプセル内のガスの種類及
び/または圧力を調整しつつ焼結性材料を加熱加圧する
方法であり、カプセル内の圧力を調整しつつ加熱加圧処
理できるため極めて有用である。In the HIP method, a sinterable material is enclosed in an airtight container called a capsule and inserted into a high-pressure container, and the sinterable material is heated by an electric heating element incorporated in the high-pressure container while the pressure in the high-pressure container is increased. At the time of applying so-called HIP for pressurizing by a isotropic compression force of a medium, for example, pressure medium gas, an adjusting pipe line that communicates with the inside of the capsule and extends its end to the outside of the high-pressure container is provided. This is a method of heating and pressurizing the sinterable material while adjusting the type and / or pressure of the gas in the capsule through a pipeline, and is extremely useful because the heating and pressurizing treatment can be performed while adjusting the pressure in the capsule.
(発明が解決しようとする問題点) ところが、本発明者等は、上記の方法を実際に適用する
過程で、カプセル内に封入したタール・ピッタなどの有
機材料を含む焼結材料が昇温過程で分解して生成する水
素ガスや炭化水素などとの共存系となり、この際カプセ
ルに何等かの異常がない場合にはカプセルの内外圧を調
整することによって高密度の炭素材料を得ることができ
るが、カプセルに例えば溶接欠陥やピンホールが存在し
た場合、あるいは圧縮過程でクラックが発生した場合な
ど、上記分解ガスがカプセル外に流出し、カプセル外の
圧媒ガス、例えば通常はアルゴンガスの中の水素濃度が
正規の状態に比して著しく増大し、高圧容器に水素脆化
あるいは水素侵食に基づく破壊を惹き起こす危険性が生
じ、高圧ガス装置としては安全上、極めて重大な問題と
なること、また、漏出した炭化水素は更に分解して、分
解カーボンが電熱装置部に付着し絶縁破壊を生じたり、
電熱装置その他の構造材料の破損を招くことなどを経験
した。(Problems to be Solved by the Invention) However, in the process of actually applying the above method, the present inventors have found that a sintering material containing an organic material such as tar and pitta encapsulated in a capsule is heated. It becomes a coexisting system with hydrogen gas and hydrocarbons that are generated by decomposing at 1. At this time, if there is no abnormality in the capsule, a high density carbon material can be obtained by adjusting the internal and external pressure of the capsule. However, when there are welding defects or pinholes in the capsule, or when cracks occur during the compression process, etc., the above-mentioned decomposed gas flows out of the capsule, and a pressure medium gas outside the capsule, for example, in argon gas is usually used. The hydrogen concentration in the high-pressure container increases significantly compared to the normal state, and there is a risk of causing hydrogen embrittlement or damage due to hydrogen erosion in the high-pressure container. It becomes a serious problem for the first time, and the leaked hydrocarbon is further decomposed, and the decomposed carbon adheres to the electric heating device part, causing dielectric breakdown,
We experienced that the electric heating device and other structural materials were damaged.
このような状況下で上記の危険性や問題点を回避し、実
用上、完璧な安全性を保証されたHIP法ならびに装置
の開発は大きな技術的課題となった。Under such circumstances, development of a HIP method and an apparatus which avoids the above-mentioned dangers and problems and guarantees practically perfect safety has become a major technical issue.
すなわち、本発明は上述の技術的課題を解決するために
鋭意研究の末、完成されたもので、その目的とするとこ
ろは、カプセル内において水素ガス,炭化水素など活性
なガスとの共存系にある焼結性材料、特に炭素材料をH
IP処理に付して高密度焼結材を得るに際し、HIP装
置またはその構造材料の損壊の危険性を完全に排除し、
安全な作業を保証するにある。That is, the present invention has been completed after intensive research to solve the above technical problems, and its purpose is to provide a coexisting system with an active gas such as hydrogen gas or hydrocarbon in a capsule. Some sinterable materials, especially carbon materials
Completely eliminates the risk of damage to the HIP device or its structural material when obtaining a high-density sintered material by IP treatment,
To ensure safe work.
他の目的は、非常制御機構すなわち安全装置を作動せし
めるに当たって装置の損傷を防止するにある。Another object is to prevent damage to the device in activating the emergency control mechanism or safety device.
(問題点を解決するための手段) 上記目的を達成するための本発明方法の特徴とするとこ
ろは、焼結性材料を水素ガス,炭化水素など活性なガス
との共存系においてカプセル内に収納し、高圧容器内で
熱間静水圧プレス処理を施すに際し、カプセルの内圧(P
1)と外圧(P2)との差(P2−P1)の値を設定値と比較して得
られた出力信号により(P1)および(P2)の値の少なくとも
一つを制御する手段を機能せしめて前記差圧を適正レベ
ルに維持する方法において、前記差圧値が予め定められ
た最小限界値に達成したとき非常出力信号により高圧容
器内の電熱装置への熱の供給を遮断するとともにカプセ
ル内のガスを独立した調整管路を経て外気へ放出するこ
とにある。(Means for Solving the Problems) A feature of the method of the present invention for achieving the above-mentioned object is that the sinterable material is contained in a capsule in a coexisting system with an active gas such as hydrogen gas or hydrocarbon. When performing hot isostatic pressing in a high-pressure container, the internal pressure (P
1 ) and the external pressure (P 2 ) difference (P 2 −P 1 ) value is compared with the set value to control at least one of the (P 1 ) and (P 2 ) values. In the method for operating the means for maintaining the differential pressure at an appropriate level, the supply of heat to the electric heating device in the high pressure vessel is provided by the emergency output signal when the differential pressure value reaches a predetermined minimum limit value. It is to cut off and release the gas in the capsule to the outside air through an independent adjusting pipe.
また、上記本発明方法の実施に供される装置は第1〜3
図に概要を示しているが、高圧円筒(1)と上下の蓋(2)
(3)とによって画成される高圧容器とその内部に断熱層
(6)を介して配設された電熱体(4)(4´)で画成される炉
室(7)とよりなり、該電熱体(4)(4´)に電力を供給する
手段と高圧容器内に圧媒ガスを供給する手段とを具えた
高温高圧装置であって、前記炉室(7)内に配置され且つ
圧媒ガスに対して気密なカプセルにその内部と連通し高
圧容器外へその端部が延長するカプセル内ガス調整管路
を接続するとともに、炉室内圧媒ガス圧(P2)およびカプ
セル内ガス圧(P1)をそれぞれ検出する検知部(19)(20)
と、検出された圧力値の差(P2−P1)を設定値と比較して
出力信号に変換するプロセッサ(28)と、該信号により前
記電力の供給量,圧媒ガスの供給量及びカプセル内ガス
排出量の少なくとも一つを制御し前記差圧値を適正レベ
ルに維持する制御機構とを具えた熱管静水圧プレス装置
を基本構成とし、前記圧力値の差を予め定められた最小
限界値に到達したときの非常出力信号により電熱体への
電力供給を遮断するとともに、前記調整管路を開放する
非常制御機構を付設せしめた高密度焼結体の製造装置で
ある。The apparatus used for carrying out the method of the present invention is the first to third
High pressure cylinder (1) and top and bottom lids (2)
(3) A high-pressure vessel defined by and a heat insulation layer inside
(6) and a furnace chamber (7) defined by the heating element (4) (4 '), and means for supplying electric power to the heating element (4) (4') A high-temperature high-pressure device comprising means for supplying a pressure medium gas into the high-pressure container, wherein the high-pressure container is arranged in the furnace chamber (7) and communicates with the inside of a capsule that is airtight to the pressure-medium gas. A detector (19) (20) that connects the gas adjustment pipe in the capsule whose end extends to the outside and detects the pressure gas (P 2 ) in the furnace chamber and the gas pressure (P 1 ) in the capsule, respectively.
And a processor (28) that compares the detected pressure value difference (P 2 −P 1 ) with a set value and converts it into an output signal, and the signal supplies the power supply amount, the pressure medium gas supply amount, and A hot-tube hydrostatic pressing device having a control mechanism for controlling at least one of the gas discharge amount in the capsule to maintain the differential pressure value at an appropriate level is used as a basic configuration, and the difference between the pressure values is set to a predetermined minimum limit. It is an apparatus for producing a high-density sintered body, which is provided with an emergency control mechanism for cutting off the electric power supply to the electric heating body by an emergency output signal when reaching the value and opening the adjusting pipe.
以下、本発明製造方法の具体的な態様を本発明装置の実
施例と共に添付図面に基づいて詳述する。Hereinafter, specific embodiments of the manufacturing method of the present invention will be described in detail with reference to the accompanying drawings together with examples of the apparatus of the present invention.
第1図は本発明方法を実施するに適切な高温高圧装置す
なわちHIP装置の本体部分及びその内部に配置した被
処理体の断面を示す。FIG. 1 shows a cross section of a main body of a high-temperature high-pressure apparatus suitable for carrying out the method of the present invention, that is, a HIP apparatus, and an object to be processed arranged therein.
図において、高圧容器は高圧円筒(1)およびその上下端
部を塞ぐ上蓋(2)と下蓋(3)とによって区画構成され、各
々の嵌合部はシール(10)(10´)によって気密に保持され
ており、蓋部に作用するガス圧力はプレス枠体(図示せ
ず)によって支持される。そして高圧容器内部には焼結
性材料よりなる被処理体(13)を加熱昇温するための電気
加熱抵抗線よりなる電熱体(4)(4´)およびこれら電熱体
からの熱により高圧円筒(1)や上蓋(2),下蓋(3)への熱
の散逸を抑制する断熱層(6)が組み込まれている。In the figure, the high-pressure container is partitioned by a high-pressure cylinder (1) and an upper lid (2) and a lower lid (3) that close the upper and lower ends thereof, and each fitting portion is hermetically sealed by a seal (10) (10 '). The gas pressure acting on the lid is supported by a press frame (not shown). Inside the high-pressure container, an electric heating element (4) (4 ') consisting of an electric heating resistance wire for heating and heating the object (13) made of a sinterable material and a high-pressure cylinder by heat from these electric heating elements A heat insulating layer (6) that suppresses the dissipation of heat to the (1), upper lid (2), and lower lid (3) is incorporated.
被処理体(13)は金属材料からなるカプセル(12)の中に収
納される。カプセル(12)にはカプセル内ガス調整用管(1
4)が取り付けられており、この管(14)は継手(15)を介し
て下蓋(3)に設けられたカプセル内ガス調整孔(11)に連
通する如く着脱自在かつ炉室(7)内の圧媒ガスとはシー
ルリング(16)により気密を保つように接続され、独立し
た調整管路が形成されている。The object to be processed (13) is housed in a capsule (12) made of a metal material. The capsule (12) has a gas adjustment tube (1
4) is attached, and this pipe (14) is detachable so as to communicate with the gas adjusting hole (11) in the capsule provided in the lower lid (3) via the joint (15) and the furnace chamber (7) It is connected to the pressure medium gas inside by a seal ring (16) so as to maintain airtightness, and an independent adjusting conduit is formed.
被処理体(13)はたとえば石油コークス,アンスラセンコ
ークス,炭素繊維などの炭素系フィラー材と、コールタ
ール・ピッチやフェノールなどの有機材料バインダーと
の混合物からなる焼結性材料の成形体である。一方、カ
プセル(12)の材料としては軟鋼,ステンレス鋼などの鋼
材の外、白金,パラジウムなど勿論、使用可能である。The object to be treated (13) is a compact of a sinterable material made of a mixture of a carbon-based filler material such as petroleum coke, anthracene coke, carbon fiber and an organic material binder such as coal tar pitch or phenol. . On the other hand, as the material of the capsule 12, not only steel materials such as mild steel and stainless steel but also platinum and palladium can be used.
又、調整管路(14)は前記カプセル(12)と同一材質又は継
手(15)との結合と容易さ等から鋼材が通常、使用され製
作される。そして、この管(14)の内部には処理時に圧媒
ガスの圧力による圧潰で閉塞すうことがなうよう難焼結
性のセラミック粉末(14)が充填される。Further, the adjusting pipe (14) is usually made of a steel material because it is made of the same material as the capsule (12) or can be easily combined with the joint (15). Then, the inside of the tube (14) is filled with a ceramic powder (14) which is difficult to sinter so as not to be clogged by being crushed by the pressure of the pressure medium gas during processing.
カプセル内ガス調整用管(14)と調整孔(11)との接合部に
はセラミッス粉末が低温部になり液分と固結するのを防
止するため金網フィルターが設けられる。A wire mesh filter is provided at the joint between the in-capsule gas adjusting tube (14) and the adjusting hole (11) in order to prevent the ceramic powder from becoming a low temperature part and solidifying with the liquid component.
本発明における炭素タール・ピッチなどの有機材料との
混合成形体はHIP処理過程で昇温すると分解して水
素,炭化水素の各ガス成分を発生する。このような物質
は通常のカプセルに封入する方法で処理すれば上記ガス
成分によりカプセル内部の圧力が上昇してカプセル外側
の不活性雰囲気ガスの圧力で十分に圧縮できなかった
り、カプセルが破裂してしまうため高密度下できないば
かりか前述の危険を招くことがある。The mixed compact with the organic material such as carbon tar and pitch in the present invention is decomposed when the temperature is raised in the HIP treatment process to generate hydrogen and hydrocarbon gas components. If such a substance is treated by an ordinary encapsulation method, the pressure inside the capsule rises due to the above gas components, and it cannot be sufficiently compressed by the pressure of the inert atmosphere gas outside the capsule, or the capsule bursts. Therefore, not only the high density cannot be achieved, but the above-mentioned danger may occur.
そこで、カプセル内外の圧力をHIP処理中に制御する
ことが求められ、これによって上記の如き成形体は高密
度製品化が可能となる。Therefore, it is required to control the pressure inside and outside the capsule during the HIP treatment, which enables the above-mentioned molded product to be made into a high-density product.
かかる圧力の制御はカプセル内外の圧力差を検知し、設
定値と比較し、その結果を調整管路作動系又は温度,圧
力調整系を指令することにより行うことができ、かかる
カプセル内圧力及び圧媒ガス圧力を制御するための配管
系統図を第2図に示す。Such pressure control can be performed by detecting the pressure difference between the inside and outside of the capsule, comparing the result with a set value, and instructing the result to the adjustment pipeline operation system or the temperature / pressure adjustment system. A piping system diagram for controlling the medium gas pressure is shown in FIG.
高圧容器(1)に対する圧媒ガス、例えばアルゴンガスの
供給のため、アルゴンガス集合装置(17)よりコンプレッ
サ(18)を通じ圧媒ガス導入孔(8)に連結される配管が設
けられ、供給圧(P2)の検知部すなわち圧力計(19)がコン
プレッサの出力側に取り付けられる。この圧媒ガス供給
系には塞止弁を適宣に配して圧媒ガス回収配管を連結し
て併設し、それぞれ独立した回路を形成することができ
る。また高圧容器は内部を真空引きするた上蓋の真空引
き用穴(9)へ通ずる真空ポンプ(25)をも具える。In order to supply pressure medium gas, for example, argon gas to the high-pressure container (1), a pipe connected to the pressure medium gas introduction hole (8) from the argon gas collecting device (17) through the compressor (18) is provided, and the supply pressure is increased. The detector (P 2 ) or pressure gauge (19) is attached to the output side of the compressor. A blocking valve may be appropriately arranged in this pressure medium gas supply system, and pressure medium gas recovery pipes may be connected and provided side by side to form independent circuits. Further, the high-pressure container also has a vacuum pump (25) which communicates with a vacuum drawing hole (9) in the upper lid for vacuuming the inside.
一方、カプセルからの調整管路は、カプセル内ガス調整
孔(11)に接続された配管により塞止弁(22)を介して外気
と流通可能となっており、また、塞止弁(23)を経て真空
ポンプ(21)と連結される。さらに調整孔と前記圧媒ガス
供給系とは逆止弁(27)および塞止弁(24)を直列に経由し
て連結されており、その管路にカプセル内圧力(P1)の検
知部である圧力計(20)を具える。On the other hand, the adjusting pipe from the capsule can be communicated with the outside air through the stop valve (22) by the pipe connected to the gas adjusting hole in the capsule (11), and the stop valve (23). And is connected to the vacuum pump (21). Further, the adjustment hole and the pressure medium gas supply system are connected via a check valve (27) and a stop valve (24) in series, and a detection unit for detecting the pressure inside the capsule (P 1 ) is provided in the conduit. It is equipped with a pressure gauge (20).
圧力計(19),(20)でそれぞれ検知された圧力(P2)および
(P1)は電気信号によって、差圧検出機能及び設定値との
比較機能ならびその結果を出力信号に変換する機能を備
えたプロセッサ例えば電子的プロセッシング回路(28)へ
入力され、プロセッサよりの出力信号は、電熱体への電
力供給制御機構,塞止弁(22)の作動機構,コプレッサ(1
8)の動力系へ選択的に送られる。Pressure (P 2 ) detected by pressure gauges (19), (20) and
(P 1 ) is input to a processor, for example, an electronic processing circuit (28) having a function of detecting a differential pressure and a function of comparing with a set value and a function of converting the result into an output signal by an electric signal, and outputs from the processor. The signals are the power supply control mechanism to the electric heating element, the operation mechanism of the stop valve (22), the copressor (1
It is selectively sent to the power system of 8).
この場合、プロセッサとしては圧力検知部即ち圧力計(1
9),(20)それぞれからの電気的信号を受ける電気式差圧
検出器のみならず、直接カプセル内外圧の差圧(P2−P1)
を検出する機械式差圧検出器をも使用することができ、
それらの検知信号を電子的回路または流体機構により出
力信号に加工する公知の機構が適宜に用いられる。In this case, as the processor, the pressure detection unit or pressure gauge (1
9), (20) Not only an electric differential pressure detector that receives electrical signals from each, but also a direct differential pressure (P 2 −P 1 )
You can also use a mechanical differential pressure detector to detect
A known mechanism for processing the detection signals into an output signal by an electronic circuit or a fluid mechanism is appropriately used.
(作 用) 次に、上記装置により成形体の高密度化を行う手順なら
びに作用について説明するが、焼結性炭素材料の成形体
は種々の方法により製造が可能である。例えば、石油コ
ークス粉末に20〜30重量部のコールタール・ピッチ
を混合し100℃前後で捏合し金型にて成形する。(Operation) Next, a procedure and an operation for densifying a compact by the above-mentioned apparatus will be described. The compact of the sinterable carbon material can be manufactured by various methods. For example, 20 to 30 parts by weight of coal tar pitch is mixed with petroleum coke powder, and the mixture is kneaded at about 100 ° C. and molded with a mold.
又、炭素繊維を使用し、かつ異方性を余り持たせない場
合には適量のタールピッチ等のバインダーを混合した
後、冷間又は温間で静水圧成形することにより目的が達
成される。又、樹脂成形体を加熱し、一部を炭化したも
のを成形体に用いることも可能である。When carbon fibers are used and the anisotropy is not so large, the object is achieved by mixing an appropriate amount of a binder such as tar pitch and then isostatically molding in cold or warm. It is also possible to heat the resin molded product and partially carbonize it to use as the molded product.
そして、かかる成形体がカプセルに収納される。Then, the molded body is stored in a capsule.
カプセルに収納された焼結性材料(成形体)はその後、
第1図に示した如く炉室(7)内の台座上に気密に載置固
定される。なお電熱体保持円筒(5)に保持された電熱体
(4)(4)や断熱層(6)などが耐酸化性に乏しいモリブデン
グラファイトからなる場合にはカプセル固定時に炉室
(7)内に混入した空気を排出するため真空引き用穴(9)を
通じ高圧容器内を真空排気する。その後、必要に応じ圧
媒ガス導入孔(8)から圧媒ガスを数〜数10kgf/cm2導
入,排出して高圧容器内のガスを置換洗浄する。The sinterable material (molded body) stored in the capsule is then
As shown in FIG. 1, it is airtightly mounted and fixed on the pedestal in the furnace chamber (7). The heating element held in the heating element holding cylinder (5)
(4) When the (4) and the heat insulation layer (6) are made of molybdenum graphite, which has poor oxidation resistance, the furnace chamber should be fixed when the capsule is fixed.
(7) The inside of the high pressure vessel is evacuated through the evacuation hole (9) in order to exhaust the air mixed therein. Thereafter, if necessary, a pressure medium gas of several to several tens kgf / cm 2 is introduced and discharged from the pressure medium gas introduction hole (8) to replace and clean the gas in the high-pressure container.
次いで、圧媒ガスを充填し、徐々に昇温を開始する。こ
のとき昇温の初期、即ち100℃強に至るまでの期間
は、カプセル内を真空引きすることによりカプセルの内
表面や焼結性材料に吸着された水分を除去することが好
ましい。更に、引き続き加熱し、昇温するとバインダー
の重合及び炭化が始まるが高密度化の製品を得るために
は重合開始後、カプセル外側からの圧媒ガスの圧力によ
り圧縮することと、バインダー成分中の炭素生成成分、
例えば炭化水素が最終的に炭素と水素にまで分解し、こ
の炭素が成形体の空隙中にできるだけ多く残留するこ
と、即ち、炭素の収率を向上させるような操作を行うこ
とが好ましい。後者の観点からはカプセル内に数10kg
f/cm2のArガスを充填した状態で昇温することにより
良い結果が得られる。Next, the pressure medium gas is filled and the temperature rise is gradually started. At this time, it is preferable to remove the moisture adsorbed on the inner surface of the capsule and the sinterable material by evacuation of the inside of the capsule during the initial period of temperature increase, that is, until reaching a temperature of over 100 ° C. Further, when the mixture is further heated and heated, the polymerization and carbonization of the binder starts, but in order to obtain a densified product, after the polymerization is started, compression by the pressure of the pressure medium gas from the outside of the capsule and Carbon producing components,
For example, it is preferable that the hydrocarbon finally decomposes into carbon and hydrogen, and that this carbon remains in the voids of the molded body as much as possible, that is, an operation that improves the yield of carbon is performed. From the latter point of view, several tens of kilograms in a capsule
Good results are obtained by raising the temperature with f / cm 2 of Ar gas filled.
このカプセル内の圧力(P1)は昇温時のArガスの膨張を伴
う圧力上昇及びバインダーが分解して発生するガス成分
の圧力により変動するので、前記の被処理体、即ち焼結
性材料成形体の圧縮のための圧縮ガスの圧力(P2)はこの
カプセル内圧力より高く保持する必要がある。特に45
0℃前後からはバインダーの分解により生成するガス
(主としてCH4)の圧力が急激に上昇し、カプセル内の
圧力(P1)が圧媒ガス圧(P2)より高くなってカプセルを破
損することがないように注意が必要である。Since the pressure (P 1 ) in this capsule fluctuates due to the pressure increase accompanying the expansion of Ar gas at the time of temperature rise and the pressure of the gas component generated by the decomposition of the binder, the above-mentioned object to be processed, that is, the sinterable material The pressure (P 2 ) of the compressed gas for compressing the molded body needs to be kept higher than the pressure inside the capsule. Especially 45
From around 0 ° C, the pressure of the gas (mainly CH 4 ) generated by the decomposition of the binder rises sharply, the pressure inside the capsule (P 1 ) becomes higher than the pressure medium gas pressure (P 2 ) and the capsule is damaged. Be careful not to let it happen.
第2図に示したカプセル内圧力及び雰囲気を制御するた
めの配管系統図において、先ず初期におけるカプセル内
部の真空排気は塞止弁(22)及び塞止弁(24)を閉じた状態
で塞止弁(23)を開き、真空ポンプ(21)を運転して行う。In the piping system diagram for controlling the pressure and atmosphere in the capsule shown in FIG. 2, first, the vacuum exhaust in the capsule in the initial stage is stopped with the stop valve (22) and the stop valve (24) closed. Open the valve (23) and operate the vacuum pump (21).
カプセル内に数10kgf/cm2のArを導入する操作は、
塞止弁(22),塞止弁(23)を閉じ、塞止弁(24)を開き、炉
室へのアルゴンガスの流入と同時に流入させるのが好ま
しい。こののち、塞止弁(24)は閉じられ、所定の昇温昇
圧操作が行われる。The operation of introducing several tens of kgf / cm 2 of Ar into the capsule is
It is preferable that the stop valves (22) and (23) are closed, the stop valve (24) is opened, and the argon gas is allowed to flow into the furnace chamber at the same time. After this, the stop valve (24) is closed, and a predetermined temperature raising / pressurizing operation is performed.
カプセル内圧力(P1)と炉室内圧媒ガスの圧力(P2)との関
係の制御、即ち、圧媒ガスによる被処理体の圧縮力の制
御は、圧縮ガスの圧力系統に設けられた圧力計(19)と、
カプセル内圧力系統に設けられた圧力計(20)の指示値を
プロセッサで比較しつつ行うことにより実現が可能であ
る。The control of the relationship between the pressure in the capsule (P 1 ) and the pressure of the pressure medium gas in the furnace (P 2 ), that is, the control of the compression force of the object to be processed by the pressure medium gas, was provided in the pressure system of the compressed gas. A pressure gauge (19),
It can be realized by comparing the indicated value of the pressure gauge (20) provided in the capsule pressure system with the processor.
昇温過程で両者の差(P1−P1)が所期の設定値より小さく
なりつつある時には、コンプレッサ(18)を駆動して圧媒
ガスの圧力(P2)を増加させるか、塞止弁(22)を開いてカ
プセル内のガス圧力(P1)を低下させることにより圧力差
(P2−P1)の適正レベルにおける維持が可能である。When the difference between the two (P 1 -P 1 ) is becoming smaller than the set value during the temperature rising process, the compressor (18) is driven to increase the pressure of the pressure medium gas (P 2 ) or to close it. By opening the stop valve (22) and decreasing the gas pressure inside the capsule (P 1 ) the pressure difference
It is possible maintenance in (P 2 -P 1) of the proper level.
処理工程の中期以降において、炭素の収率を向上するに
は、昇温速度を制御する方が効果的であるが、これは、
カプセル内圧力系統にある圧力計(20)の指示値の変化を
見ながら電熱体(4)(4´)への投入電力を制御することに
より、容易に実現される。From the middle stage of the treatment process, it is more effective to control the heating rate in order to improve the carbon yield.
This can be easily realized by controlling the input power to the electric heating elements (4) (4 ') while observing the change in the indicated value of the pressure gauge (20) in the capsule pressure system.
又、上記投入電力制御を自動的に行うには加熱電力制御
装置を利用し、これに圧力計(20)からの圧力信号を圧力
電気信号線によりプロセッサを経て同装置内に取り込む
ようにすると共に、所期の圧力設定値とこの圧力信号値
とを比較し設定値より小さい場合には投入電力を増加さ
せ、逆の場合には減少させる制御装置を組み込めば充
分、その目的を達成することができる。Further, in order to automatically perform the input power control, a heating power control device is used, and a pressure signal from the pressure gauge (20) is taken into the device through a processor through a pressure electrical signal line. , If the target pressure set value is compared with this pressure signal value, and if it is less than the set value, the input power is increased, and in the opposite case, a control device that increases it is sufficient to achieve the purpose. it can.
昇温過程でカプセル内圧力(P1)と炉室内圧媒ガスの圧力
(P2)との差(P2−P1)が極端に小さくなった場合、例え
ば、20kgf/cm2より小さくなった場合は、カプセ
ルの破裂を防止するという点からも、又、カプセルの気
密性が何等かの理由で破壊された可能性に対処するとい
う点からも緊急に装置の運転を停止することが必要であ
る。従って、差圧(P2−P1)に対する適宜な最小限界値、
例えば20kgf/cm2を設定しておき、圧力計(19)と圧
力計(20)とからの電気的信号を受けた差圧検出器(28)な
どの差圧検出機能及び比較機能を具えたプロセッサから
の出力信号によって電熱体への電力投入を遮断するとと
もに塞止弁(22)を開き、カプセル内の分解ガスを調整管
路を経由して外気に放出すると共に、カプセルに異常が
あったときは、炉室内圧媒ガス、例えばアルゴンガスを
カプセル内部を通じ大気へ放出する径路を形成してカプ
セル内の分解ガスが炉室内に流出するの抑止する。Pressure in the capsule (P 1 ) and pressure of pressure medium gas in the furnace
If the difference between (P 2) (P 2 -P 1) becomes extremely small, for example, if it is smaller than 20 kg f / cm 2, from the viewpoint of preventing rupture of the capsule, and, There is also an urgent need to shut down the device in order to deal with the possibility that the hermeticity of the capsule has been destroyed for some reason. Therefore, appropriate minimum limit value for the pressure difference (P 2 -P 1),
For example, 20 kgf / cm 2 is set in advance, and a differential pressure detection function and a comparison function such as a differential pressure detector (28) which receives an electric signal from the pressure gauge (19) and the pressure gauge (20) are provided. The output signal from the processor cuts off the power supply to the heating element and opens the shut-off valve (22) to release the decomposed gas in the capsule to the outside air through the adjustment pipe and there was an abnormality in the capsule. At this time, a path for releasing the pressure medium gas in the furnace chamber, for example, argon gas, to the atmosphere through the inside of the capsule is formed to prevent the decomposed gas in the capsule from flowing out into the furnace chamber.
なお、上記ガス放出を余り急速に行うと、高圧容器内部
に構造物が破損したり、あるいは高温ガスの通過に基づ
く配管系の破損が生じたりするので、調整管路に流速を
制限するための絞り弁(26)を設けるとことが好適であ
る。If the gas is released too quickly, the structure may be damaged inside the high-pressure vessel or the piping system may be damaged due to the passage of high-temperature gas. It is preferable to provide a throttle valve (26).
さらに、必要い応じて放出配管系、即ち、調整管路の水
冷却を行うなどの冷却手段を設けたり、あるいは第3図
に示す如く調整管路に塞止弁(29)を介して高圧室の低温
部と連通する配管系(30)を設け、塞止弁(22)が開放され
ると同時に塞止弁(29)をも開放するように構成すること
が、装置保護の観点からは好ましい。Further, if necessary, a discharge pipe system, that is, a cooling means such as water cooling of the adjusting pipe is provided, or the adjusting pipe is provided with a high pressure chamber through a blocking valve (29) as shown in FIG. It is preferable from the viewpoint of device protection that a pipe system (30) communicating with the low temperature part of the device is provided, and the stop valve (22) is opened and the stop valve (29) is opened at the same time. .
なお、以上述べた非常制御機構すなわち安全装置は、第
2図に示す如くカプセル内と高圧容器内とを連通する配
管系が存在する場合には、塞止弁(24)が閉のときにのみ
機能させるべきであるので、塞止弁(24)の閉の信号とカ
プセル内外の差圧限界信号とをもって塞止弁(22)の開放
措置がとられるように構成することがよい。The emergency control mechanism, that is, the safety device described above, can be used only when the blocking valve (24) is closed when there is a piping system for communicating the inside of the capsule with the inside of the high pressure container as shown in FIG. Since it should function, it is preferable that the closure valve (22) be opened based on the closure signal of the closure valve (24) and the differential pressure limit signal inside and outside the capsule.
これに加えるに、高圧容器内の断熱層(6)を倒立コップ
型の気密性ケーシング、即ち、ハロゲン乃至ヘリウムデ
ィテクタではリーク部が検出されない程度の気密性を有
するケーシングで構成することは、圧媒ガスとして通
常、よく用いられるアルゴンガスよりも軽い水素ガス
を、仮にカプセルより流出してもケーシング内上部に滞
留させ、直ぐには圧力容器壁に到達させないという点
で、特に水素ガスに対する付加的安全装置として好適で
ある。In addition to this, the heat insulating layer (6) in the high-pressure vessel is composed of an inverted cup-type airtight casing, that is, a casing having an airtightness such that a leak is not detected by a halogen or helium detector. Hydrogen gas, which is usually lighter than argon gas, is retained in the upper part of the casing even if it outflows from the capsule and does not reach the pressure vessel wall immediately. Is suitable as
さらに圧媒ガス中の水素濃度を処理過程において適宜サ
ンプリング分析し、水素濃度が規定値以上となった場
合、加熱装置への電力投入を断つという措置が講ずるこ
とは、より一層安全な装置となすという点で好ましいこ
とである。Furthermore, it is a safer device to take appropriate measures such as sampling and analyzing the hydrogen concentration in the pressure medium gas during the treatment process, and if the hydrogen concentration exceeds the specified value, cut off the power supply to the heating device. This is preferable in that respect.
なお、以上は焼結性材料として炭素材料を処理するHI
P装置の安全装置として説明を行ったが水素ガスをカプ
セル内に投入しつつ、カプセル内の焼結性材料を水素ガ
スとの共存系で圧縮処理する、他の処理目的をもった方
法並びに装置等にも本発明を適用し得ることは言うまで
もない。It should be noted that the above is HI for treating a carbon material as a sinterable material
Although it has been described as a safety device for the P device, a method and a device for other processing purposes, in which the sinterable material in the capsule is compressed in a coexisting system with hydrogen gas while introducing hydrogen gas into the capsule. It goes without saying that the present invention can be applied to the above.
(実施例) 平均粒径20μmの石油コークス70重量部にコールタ
ールピッチ30重量部を加え、140℃にて捏合した
後、室温まで冷却し粉砕した。得られた粉末をゴム袋に
入れ、ラバープレス装置により3000kgf/cm2の圧
力にて成形した。旋削により得られた円柱状のサンプル
(直径50mm×高さ50mm,重量126.9g)を、軟
鋼カプセルに収納した。このカプセルを第1図に示した
ような状態で高温高圧装置に装着した。装置の炉室内を
真空引き、アルゴンガス置換した後、120kgf/cm2
のアルゴンガスを炉室内に充填し、温度及び炉室内圧力
を変化させて成形体を圧縮炭化させた。(Example) 30 parts by weight of coal tar pitch was added to 70 parts by weight of petroleum coke having an average particle size of 20 μm, and the mixture was kneaded at 140 ° C., then cooled to room temperature and ground. The obtained powder was put in a rubber bag and molded by a rubber press machine at a pressure of 3000 kgf / cm 2 . A cylindrical sample (diameter 50 mm × height 50 mm, weight 126.9 g) obtained by turning was placed in a mild steel capsule. This capsule was mounted in a high temperature and high pressure apparatus in the state as shown in FIG. After the inside of the furnace of the equipment is evacuated and replaced with argon gas, 120 kgf / cm 2
Was charged into the furnace chamber, and the temperature and pressure in the furnace chamber were changed to compress and carbonize the molded body.
この時、カプセル内の圧力は、制御回路により主として
大気圧へ解放するための塞止弁を自動操作し、0〜20
0kgf/cm2の範囲を越えないよう、かつ、圧媒ガスの
炉内圧力との差が100kgf/cm2をレベルを越えない
ように調節した。At this time, the pressure in the capsule is automatically controlled by the control circuit to automatically operate the stop valve for releasing it mainly to the atmospheric pressure.
The pressure was adjusted so that the range of 0 kgf / cm 2 was not exceeded, and the difference between the pressure of the pressure medium gas and the furnace pressure was 100 kgf / cm 2 so as not to exceed the level.
降温,降圧後、軟鋼カプセルを取り除き焼成体を取り出
した。得られた焼結体の寸法及び重量は直径44mm,高
さ45mm,重量107.4gであった。嵩密度は、1.56
g/cm2で、クラックの発生も軽微であった。After cooling and lowering the pressure, the mild steel capsule was removed and the fired body was taken out. The size and weight of the obtained sintered body were 44 mm in diameter, 45 mm in height, and 107.4 g in weight. Bulk density is 1.56
The generation of cracks was also slight at g / cm 2 .
次いで、同一条件で成形した焼結性材料を同様に高温高
圧装置に装着し、電熱体への投入電力を増加し、急激な
温度上昇を行うとともに、圧媒ガスの圧力上昇速度を故
意に低下させて運転を行った。Next, a sinterable material molded under the same conditions was similarly installed in a high temperature and high pressure device to increase the electric power input to the electric heating element to rapidly raise the temperature and intentionally reduce the pressure rising rate of the pressure medium gas. Let me drive.
カプセルの内外圧の差の標準値を100kgf/cm2と
し、また最小限界値を50kgf/cm2と設定したとこ
ろ、温度450℃付近で成形体の急激な分解によりガス
発生のため、ガス放出量と均衡が崩れ、自動制御限界を
越えて圧力差が50kgf/cm2に到達し、非常制御機構
が働いたが。それにより電熱体への通電が停止すうとと
おもに調節管路が全開したため非常自体を回避すること
ができた。When the standard value of the difference between the internal pressure and the external pressure of the capsule was set to 100 kgf / cm 2 and the minimum limit value was set to 50 kgf / cm 2 , the amount of gas released due to the rapid generation of gas around the temperature of 450 ° C due to the rapid decomposition of the compact. However, the balance became unbalanced, the pressure difference reached 50 kgf / cm 2 beyond the automatic control limit, and the emergency control mechanism worked. As a result, the control conduit was fully opened when the power supply to the electric heating element was stopped, and the emergency itself could be avoided.
その後、炉内圧媒ガスのサンプリングと分析とにより水
素ガスの混入が検出されなかったため、温度,圧力の上
昇プログラムを正常に戻して、前記同様の焼結体を取得
した。After that, since the mixing of hydrogen gas was not detected by the sampling and analysis of the pressure medium gas in the furnace, the temperature and pressure increase programs were returned to normal, and a sintered body similar to the above was obtained.
(発明の効果) 本発明は以上のように炭素とタールピッチなどの有機材
料からなる焼結性成形体を焼成するにあたり、カプセル
内ガス調整管路を有する金属からなるカプセルを使用
し、該カプセル内に前記成形体を収納し、カプセル外側
圧力で圧縮しつつ昇温し、同時にカプセル内外の圧力差
を検出して、その値を適正レベルに維持しつつ焼結する
に際し、発生ガスによる内圧の上昇,カプセルの異常変
形等によるカプセルの隔離性能の喪失に起因する上記圧
力差の異常を逸早く検出して、ガスの発生を抑制すると
ともにカプセル内ガスを独立した調整管路によって外気
に排出する安全措置を講じたから、水素,炭化水素等の
分解ガスが圧媒ガスに混入し、高圧容器の器壁に水素脆
化あるいは水素侵食に基づく破壊を招くなどの由々しい
自体を完全に回避することができる。(Effects of the Invention) The present invention uses a capsule made of a metal having a gas adjusting pipeline in the capsule when firing a sinterable compact made of an organic material such as carbon and tar pitch as described above. The molded body is stored in the capsule, the temperature is increased while being compressed by the pressure on the outside of the capsule, and at the same time, the pressure difference between the inside and the outside of the capsule is detected. Safety that quickly detects abnormalities in the above pressure difference due to loss of the isolation performance of the capsule due to rising, abnormal deformation of the capsule, etc., suppresses gas generation, and discharges the gas inside the capsule to the outside through an independent adjustment pipeline. Since the measures were taken, the decomposition gas such as hydrogen and hydrocarbon is mixed in the pressure medium gas, which causes the embrittlement of hydrogen on the vessel wall of the high-pressure vessel or the destruction due to hydrogen erosion. Can be completely avoided.
また、炭化水素の分解によるカーボンが加熱装置部に付
着して惹き起こされる絶縁破壊や、その他の構造材料の
損傷をも未然に防止することができる。Further, it is possible to prevent the dielectric breakdown caused by the carbon adhering to the heating device portion caused by the decomposition of hydrocarbons and the damage to other structural materials.
このように本発明によれば、高強度,高密度かつ等方的
な炭素成形体を完璧な安全性をもってHIP成形により
取得することができるから、産業界多方面の需要によく
応えるとともに、本発明は高圧機器の取扱いに際して、
格別厳重な注意と配慮とを払うべき安全性を保証し、災
害,事故,損失等を未然に防止し得るという効果顕著に
して頗る有用な発明である。As described above, according to the present invention, a high-strength, high-density and isotropic carbon molded body can be obtained by HIP molding with perfect safety. The invention, when handling high-voltage equipment,
It is a useful invention that makes it possible to assure the safety that pays strict attention and attention and prevent accidents, accidents, losses, etc.
第1図は本発明方法を実施する装置の一例を示す断面概
要図、第2図はカプセル内圧力および圧媒ガス圧力制御
配管系統図、第3図は制御機構の他の例を示す本発明装
置の配管系統図である。 (1)……高圧円筒,(2)……上蓋, (3)……下蓋,(4)(4′)……電熱体, (6)……断熱層,(7)……炉室, (8)……圧媒ガス導入孔, (9)……真空引き孔, (11)……カプセル内ガス調整孔, (12)……カプセル, (13)……成形体(被処理体), (14)……カプセル内ガス調整用管路, (14)……難焼結性セラミック粉末, (15)……継手, (17)……アルゴンガス集合装置, (18)……コンプレッサ, (19)(20)……圧力計(検知部), (21)(25)……真空ポンプ, (22)(23)(24)(29)……塞止弁, (26)……絞り弁,(27)……逆止弁, (28)……プロセッサ,FIG. 1 is a schematic sectional view showing an example of an apparatus for carrying out the method of the present invention, FIG. 2 is a system diagram for controlling the pressure inside the capsule and the pressure medium gas pressure, and FIG. 3 is another example of the control mechanism of the present invention. It is a piping system diagram of an apparatus. (1) …… High-pressure cylinder, (2) …… Upper lid, (3) …… Lower lid, (4) (4 ′) …… Electric heating element, (6) …… Insulating layer, (7) …… Furnace chamber , (8) …… Pressure medium gas introduction hole, (9) …… Vacuum suction hole, (11) …… Capsule gas adjustment hole, (12) …… Capsule, (13) …… Molded body (object to be treated) ), (14) …… Conduit for gas adjustment in capsule, (14) …… Stainless ceramic powder, (15) …… Fitting, (17) …… Argon gas collector, (18) …… Compressor , (19) (20) …… Pressure gauge (detector), (21) (25) …… Vacuum pump, (22) (23) (24) (29) …… Stop valve, (26) …… Throttle valve, (27) …… Check valve, (28) …… Processor,
Claims (11)
なガスとの共存系においてカプセル内に収納し、高圧容
器内で熱間静水圧プレス処理を施すに際し、カプセルの
内圧(P1)と外圧(P2)との差圧(P2−P1)の値を設定値と比
較して得られた出力信号により(P1)および(P2)の値の少
なくとも一つを制御する手段を機能せしめて前記差圧を
適正レベルに維持する方法において、前記差圧値が予め
定められた最小限界値に到達したとき、非常出力信号に
より高圧容器内の電熱装置への熱の供給を遮断するとと
もにカプセル内のガスを独立した調整管路を経て外気へ
放出することを特徴とする高密度焼結体の製造方法。1. A sinterable material is housed in a capsule in a coexisting system with an active gas such as hydrogen gas or hydrocarbon, and when the hot isostatic pressing process is performed in a high-pressure container, the internal pressure (P 1 ) And the external pressure (P 2 ), the output signal obtained by comparing the value of the differential pressure (P 2 −P 1 ) with the set value controls at least one of the values of (P 1 ) and (P 2 ). In the method of operating the means for maintaining the differential pressure at an appropriate level, when the differential pressure value reaches a predetermined minimum limit value, supply of heat to the electric heating device in the high pressure vessel by an emergency output signal. And a gas in the capsule is discharged to the outside air through an independent adjusting pipe, and a method for producing a high-density sintered body.
許請求の範囲第1項記載の高密度焼結体の製造方法。2. The method for producing a high density sintered body according to claim 1, wherein the gas is released at a limited flow rate.
しつつ行われる特許請求の範囲第1項または第2項記載
の高密度焼結体の製造方法。3. The method for producing a high-density sintered body according to claim 1, wherein the gas is released while cooling the gas in the adjusting pipe.
器内の低温部のガスと前記調整管路内で合流せしめて行
われる前記特許請求の範囲各項の何れかに記載の高密度
焼結体の製造方法。4. The high density according to claim 1, wherein the gas is released by allowing the gas in the capsule to merge with the gas in the low temperature section in the high pressure container in the adjusting pipeline. Manufacturing method of sintered body.
部とを連通する管路の閉鎖を確認した上で作用する前記
特許請求の範囲各項の何れかに記載の高密度焼結体の製
造方法。5. The production of the high-density sintered body according to claim 1, wherein the emergency output signal is actuated after confirming the closure of the conduit connecting the interior of the capsule and the interior of the high-pressure container. Method.
高圧容器とその内部に断熱層を介して配設された電熱体
で画成される炉室とよりなり、該電熱体に電力を供給す
る手段と高圧容器内に圧媒ガスを供給する手段とを具え
た高温高圧装置であって、前記炉室内に配置され且つ圧
媒ガスに対して気密なカプセルにその内部と連通し高圧
容器外へその端部が延長するカプセル内ガス調整管路を
接続するとともに、炉室内圧媒ガス圧(P2)及びカプセル
内ガス圧(P1)をそれぞれ検出する検知部と、検出された
圧力値の差(P2−P1)を設定値と比較して出力信号に変換
するプロセッサと、該信号により前記電力の供給量,圧
媒ガスの供給量およびカプセル内ガス排出量の少なくと
も一つを制御し前記差圧値を適正レベルに維持する制御
機構とを具えた熱間静水圧プレス装置において、前記圧
力値の差が予め定められた最小限界値に到達したときの
非常出力信号により電熱体への電力供給を遮断するとと
もに前記調整管路を開放する非常制御機構を付設してな
ることを特徴とする高密度焼結体の製造装置。6. A high-pressure container defined by a high-pressure cylinder and upper and lower lids, and a furnace chamber defined by an electric heating element disposed inside the high-pressure container via a heat insulating layer, and electric power is supplied to the electric heating element. A high-temperature high-pressure device comprising means for supplying a pressure medium and a means for supplying a pressure medium gas into a high-pressure container, the high-pressure device communicating with the inside of a capsule that is arranged in the furnace chamber and is airtight to the pressure medium gas. A detection unit that detects the gas pressure inside the reactor chamber (P 2 ) and the gas pressure inside the capsule (P 1 ) while connecting the gas adjustment pipeline inside the capsule whose end extends outside the container was detected. A processor that compares the pressure value difference (P 2 −P 1 ) with a set value and converts it into an output signal, and at least one of the power supply amount, pressure medium gas supply amount, and capsule gas discharge amount by the signal. Control mechanism for controlling the pressure difference and maintaining the differential pressure value at an appropriate level. In the isostatic pressing apparatus, an emergency control mechanism that shuts off the electric power supply to the electric heating body by the emergency output signal when the difference between the pressure values reaches a predetermined minimum limit value and opens the adjustment pipeline is provided. An apparatus for producing a high-density sintered body, characterized by being attached.
求の範囲第6項記載の高密度焼結体の製造装置。7. An apparatus for producing a high-density sintered body according to claim 6, wherein the adjusting pipe comprises a throttle valve.
具えてなる特許請求の範囲第6項または第7項記載の高
密度焼結体の製造装置。8. An apparatus for producing a high-density sintered body according to claim 6 or 7, wherein said adjusting pipe is provided with a cooling means for cooling it.
低温部と連通しており、前記非常出力信号により該塞止
弁を開くようになした前記特許請求の範囲第6項乃至第
8項の何れかに記載の高密度焼結体の製造装置。9. The method according to claim 6, wherein the adjusting pipe communicates with a low temperature portion in the high pressure vessel through a stop valve, and the stop valve is opened by the emergency output signal. An apparatus for manufacturing a high-density sintered body according to any one of items 8 to 8.
て高圧容器への圧媒ガス供給配管と連結されており、前
記非常制御機構は該塞止弁の閉止を確認した上で作用す
るものである前記特許請求の範囲第6項乃至第9項の何
れかに記載の高密度焼結体の製造装置。10. The adjusting pipe is connected to a pressure medium gas supply pipe to a high-pressure container through a stop valve and a check valve, and the emergency control mechanism confirms that the stop valve is closed. 10. The apparatus for producing a high-density sintered body according to any one of claims 6 to 9, wherein the manufacturing apparatus for a high-density sintered body operates according to any one of claims 6 to 9.
グよりなる前記特許請求の範囲第6項乃至第10項の何れ
かに記載の高密度焼結体の製造装置。11. The manufacturing apparatus for a high-density sintered body according to claim 6, wherein the heat insulating layer is an inverted cup-type airtight casing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60109580A JPH0617489B2 (en) | 1985-05-21 | 1985-05-21 | Method and apparatus for manufacturing high-density sintered body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60109580A JPH0617489B2 (en) | 1985-05-21 | 1985-05-21 | Method and apparatus for manufacturing high-density sintered body |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61266503A JPS61266503A (en) | 1986-11-26 |
| JPH0617489B2 true JPH0617489B2 (en) | 1994-03-09 |
Family
ID=14513873
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60109580A Expired - Lifetime JPH0617489B2 (en) | 1985-05-21 | 1985-05-21 | Method and apparatus for manufacturing high-density sintered body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0617489B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0195286A (en) * | 1987-10-07 | 1989-04-13 | Kawasaki Heavy Ind Ltd | Hot hydrostatic pressure device |
-
1985
- 1985-05-21 JP JP60109580A patent/JPH0617489B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61266503A (en) | 1986-11-26 |
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