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JPS58162865A - Method and apparatus for estimating organic compound fluid - Google Patents

Method and apparatus for estimating organic compound fluid

Info

Publication number
JPS58162865A
JPS58162865A JP4600582A JP4600582A JPS58162865A JP S58162865 A JPS58162865 A JP S58162865A JP 4600582 A JP4600582 A JP 4600582A JP 4600582 A JP4600582 A JP 4600582A JP S58162865 A JPS58162865 A JP S58162865A
Authority
JP
Japan
Prior art keywords
sample
thin film
organic compound
storage tank
compound fluid
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
JP4600582A
Other languages
Japanese (ja)
Other versions
JPS6412341B2 (en
Inventor
Mitsuaki Iino
飯野 光明
Takao Katayama
片山 隆夫
Masayuki Nakanishi
正幸 中西
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.)
Idemitsu Kosan Co Ltd
Original Assignee
Idemitsu Kosan 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 Idemitsu Kosan Co Ltd filed Critical Idemitsu Kosan Co Ltd
Priority to JP4600582A priority Critical patent/JPS58162865A/en
Publication of JPS58162865A publication Critical patent/JPS58162865A/en
Publication of JPS6412341B2 publication Critical patent/JPS6412341B2/ja
Granted legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/26Oils; Viscous liquids; Paints; Inks
    • G01N33/28Oils, i.e. hydrocarbon liquids
    • G01N33/2805Oils, i.e. hydrocarbon liquids investigating the resistance to heat or oxidation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Biochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Food Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Sampling And Sample Adjustment (AREA)
  • Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)

Abstract

PURPOSE:To estimate oxidation life of a sample accurately and rapidly, by compulsorily deteriorating the whole sample of a liquid org. compd. circulated in a thin film. CONSTITUTION:A circulation pump 21 is actuated to draw a sample 13 from a storage tank 10 through a tube 18 and feed it to a sample introduction part 5. The sample 13 is fed to the upper part of the conical large-diameter part 2A of a funnel 2, flows down along the external peripheral surface of the part 2A, gradually formed into a thinner film, and propagated to the inner cylinder surface 1A of a glass cylinder 1 in a cylindrical thin film 6 having uniform thickness. At that time, the film 6 is deteriorated by heating the sample 13 to a temp. higher than that of it in the tank 10 with a heater 11, and further degraded by bringing it into contact with the atmospheric gas injected from an injection nozzle 8B, and rising with replacing all the gas contained in the cylinder 1. The sample 13 flows down moreover accelerated toward deterioration by contact with a catalyst 30. Oxidation life of the org. liq. compd., etc. can be thus estimated exactly and rapidly.

Description

【発明の詳細な説明】 本発明は有機化合物流体を強制的に劣化させてその劣化
直管測定することによシ有機化合物流体を評価する評価
方法および評価装置に係〕、更に詳しくは有機化合物流
体を劣化させる方法の改良およびその5j!施装置Kl
lする。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an evaluation method and an evaluation apparatus for evaluating an organic compound fluid by forcibly degrading the organic compound fluid and measuring the deterioration straight pipe. Improvements in methods of degrading fluids and their 5j! Application device Kl
I do it.

従来より、有機化合物流体を評価する方法社日本規格協
会(JIS)やアメリカ材料試験協会(ASTM)によ
るものをはじ・めとして種々提案されてお多い例えば有
機化合物流体である潤滑油の酸化寿命を評価する方法に
あっては、インディアナ酸化試験(スタンダードオイル
−インディアナ社の提案によるもの)、ロータリボンデ
酸化安定置試験(ASTM D  2272)、インデ
ィアナスターリング酸化試験(JIS  K  251
4)、タービン油酸化安定度試験(JIS  K  2
515勢)などが広く採用されている。しかしながら、
これらの試験法は全て試料である潤滑油の全体を均一的
に加熱して強制劣化させるものであり、したがって、試
料七局藻的にも200℃以上に加熱することのないもの
であつ九。
Various methods for evaluating organic compound fluids have been proposed, including those by the Japanese Standards Institute (JIS) and the American Society for Testing and Materials (ASTM). Evaluation methods include the Indiana oxidation test (proposed by Standard Oil-Indiana), the rotary ribbon oxidation stability test (ASTM D 2272), and the Indiana Stirling oxidation test (JIS K 251).
4) Turbine oil oxidation stability test (JIS K 2
515 units) etc. are widely adopted. however,
All of these test methods uniformly heat the entire sample of lubricating oil to forcefully degrade it, and therefore, the samples are not heated above 200°C.

ところが、実際に使用される潤滑油の状況は、軸受藝や
歯車表面付近等の可動16にあっては時には800℃に
も達する程の極めて高温に加熱される一方、潤滑油の1
1部中貯槽i1にあっては比較的低温度とされ、潤滑油
は高温の可動部と低温O貯槽部との閣を循環しているも
のである。し九がって、このような実際に使用される潤
滑油の状況とは極めて相違する条件下で潤滑油を強制劣
化させる前記各試験法では、潤滑油の酸化寿命を必らず
しも適正に評価することができ・ないという欠点を有し
ていた。しかも、タービン油酸化安定度試験にあっては
過t2000〜5000時間もの試験時間を要するもの
であった。また、潤滑油の酸化寿命に隈らず、油脂類等
をはじめとして有機化合物流体を適正且迅速に評価する
ことのできる評価方法および評価装置が望まれてい友。
However, the situation with lubricating oil in practice is that it is heated to extremely high temperatures, sometimes reaching 800°C, in moving parts such as bearings and near the surfaces of gears.
The temperature in the storage tank i1 in the first part is relatively low, and the lubricating oil is circulated between the high temperature moving part and the low temperature O storage tank part. Therefore, each of the test methods described above, in which lubricating oil is forcibly degraded under conditions that are extremely different from the conditions in which lubricating oil is actually used, does not necessarily guarantee the proper oxidation life of lubricating oil. It had the disadvantage of not being able to be evaluated. Moreover, the turbine oil oxidation stability test required a test time of over 2,000 to 5,000 hours. Furthermore, in addition to the oxidation life of lubricating oil, there is a need for an evaluation method and apparatus that can appropriately and quickly evaluate organic compound fluids including oils and fats.

本発明の目的は、有機化合物流体を適正且迅速に評価す
ることのできる有機化合物流体の評価方法および評価値
*’を提供するにある。
An object of the present invention is to provide an evaluation method and evaluation value *' for an organic compound fluid that can appropriately and quickly evaluate the organic compound fluid.

本発明に係る評価方法は、試料としての有機化合物流体
の−Wt−薄膜状にし友後、一旦貯槽内に導入させると
ともに、貯槽内の試料の一部を取出して再び薄膜状にす
るように試料を循環させながら主として薄膜状の試料の
劣化を促進させて試料全体を強制劣化させることにより
、実際に使用される試料の状況と条件を近似させて前記
目的を達成しようとするものである。
In the evaluation method according to the present invention, an organic compound fluid as a sample is made into a -Wt-thin film, and then introduced into a storage tank, and a part of the sample in the storage tank is taken out and the sample is made into a thin film again. The purpose is to approximate the situation and conditions of the sample actually used and achieve the above objective by accelerating the deterioration of mainly the thin film sample while circulating the sample, thereby forcibly degrading the entire sample.

また、本発明に係る評価装置は、試料としての有機化合
物流体が薄膜状となって流下される傾けられ若しくは鉛
直方向に向けられた壁面を備え次薄膜発生機構と、前記
壁面の下方側に配置され流下され一試料を収容する貯槽
と、貯槽内の試料を前記薄膜発生機構に供給する循環ポ
ンプとを設け、循環Iンデによ多試料を貯槽から薄膜発
生機構へと循環させながら、薄膜発生機構においては試
料が薄膜状にされて劣化が促進されるようにして前記目
的を達成しようとするもΩである。
Furthermore, the evaluation device according to the present invention includes a wall surface that is inclined or oriented in a vertical direction, through which the organic compound fluid as a sample flows down in the form of a thin film, and a thin film generation mechanism that is disposed on the lower side of the wall surface. A storage tank for accommodating one sample that has been washed down and a circulation pump that supplies the sample in the storage tank to the thin film generation mechanism is provided. In the generation mechanism, the above objective is achieved by making the sample into a thin film and accelerating the deterioration.

以下、本発明の実施例を図面に基づいて説明する。Embodiments of the present invention will be described below based on the drawings.

第1図には、本発明に係る有機化合物流体の評価装置の
一実施例の全体構成が示されている。この図において、
鉛直方向に沿って配置され几パイレックスガラス(商標
名)尋よりなるdラスシリン/1とガラスシリンダ1の
上端寄ルの所定の位置くおいて円錐状の大径部2^側が
鉛直下方向に向くよう、すなわち逆さに配置された漏斗
2とにより薄膜発生機構3が構成されている。
FIG. 1 shows the overall configuration of an embodiment of an organic compound fluid evaluation apparatus according to the present invention. In this diagram,
The d-las cylinder/1 made of thick Pyrex glass (trade name) is arranged along the vertical direction and placed at a predetermined position near the upper end of the glass cylinder 1, with the conical large diameter part 2^ side facing vertically downward. A thin film generating mechanism 3 is constituted by the funnel 2 and the funnel 2 which are arranged upside down.

漏斗2の細管部2Bは、ガラスシリンダ1の上端開口1
11にこの開口部を閉塵するように圧入されるテフロン
(商標名 −リテトラフルオルエチレン)樹脂等よシな
る路内柱体状のキャップ4の中心部に圧入されて貫挿保
持され且キャツf4PclIスジリンダ1の内周面に密
着されないが極めて近接された状態となるよう固定支持
されている。
The thin tube part 2B of the funnel 2 is connected to the upper end opening 1 of the glass cylinder 1.
The cap 11 is press-fitted into the center of a column-shaped cap 4 made of Teflon (trade name: Litetrafluoroethylene) resin or the like so as to close this opening, and is held through the center of the cap 4. The cat f4PclI is fixedly supported so that it is not in close contact with the inner circumferential surface of the linear cylinder 1, but is very close to it.

ま次、キャラ7″′4には試料導入部5が穿設されてお
り、この試料導入部5Fi、キャップ4の側面の所定位
置にて開口し且キャップ4の中心部まで穿設された水平
部5Aとキャップ4の下熾面中心部にて開口し且前配水
平部5Aに連通されているとともに所定の間隙を有しな
がら前記漏斗2の細管部2B’に囲繞する垂直部5Bと
によシ構成されており、水平部5Aよシ導入された試料
は垂直部5Btl−経て漏斗2の大径部2^の上端側に
流下され、この流下され次試料は大径部2Aの円錐状の
外周面を薄膜化されながら流下され、試料が薄膜状とな
って流下される壁面としての前記ガラスシリンダ1の内
周面1Aへと伝えられ次のち前記内周WJIAK沿って
薄膜状の薄膜部6となって流下される う罠なっている
。ま友、内周面IAKはコイル状の銅、鉄等よ少なる触
媒30が内周面1Aに接するよう設けられており、前記
薄膜部6は触媒30に接しながら流下される。
Next, a sample introduction part 5 is bored in the character 7'''4. part 5A and a vertical part 5B that opens at the center of the lower surface of the cap 4, communicates with the front horizontal part 5A, and surrounds the narrow tube part 2B' of the funnel 2 with a predetermined gap. The sample introduced from the horizontal part 5A flows down to the upper end side of the large diameter part 2^ of the funnel 2 through the vertical part 5Btl-, and the next sample after flowing down flows into the conical part of the large diameter part 2A. The sample is flowed down while being made into a thin film, and the sample is transferred in a thin film form to the inner peripheral surface 1A of the glass cylinder 1, which serves as the wall surface on which it flows down, and then a thin film portion is formed along the inner periphery WJIAK 6 and flow down.The inner peripheral surface IAK is provided with a coiled catalyst 30 made of copper, iron, etc., in contact with the inner peripheral surface 1A, and the thin film portion 6 flows down while contacting the catalyst 30.

ガラスシリンダ1の外周部にはガラスシリンダ1の長手
方向に沿って所定の範囲に亘り加熱機構Tが囲繞されて
いる。この加熱機構7は前記外周部に巻きつけられ次ニ
クロム線7Aと、このニクロムM7Aを覆うアスベスト
リボン(図示せず)とを有し、ま危加熱機構7には熱電
対(図示せず)が設けられており、この熱電対により加
熱機構Tの温度制御が行なわれるようになっている。
A heating mechanism T is surrounded by a predetermined range on the outer periphery of the glass cylinder 1 along the longitudinal direction of the glass cylinder 1 . This heating mechanism 7 has a nichrome wire 7A wrapped around the outer periphery and an asbestos ribbon (not shown) covering the nichrome M7A, and the heating mechanism 7 also has a thermocouple (not shown). The temperature of the heating mechanism T is controlled by this thermocouple.

ガラスシリンダ1の下端開口部にFi漏斗状の連結具8
が取付けられている。この連結具8の上端縁はガラスシ
リンダ1の下端縁と摺り合わせ部9を介して密接されて
ガス漏れ轡のないようになっているとともに、連結具8
の細管部8Aは略広口びん状の貯槽10の開口部に嵌合
されたゴム製等の蓋部11の中心部を下方に向って貫挿
されておp1連結具8によりガラスシリンダ1内と貯槽
10内とが連通されている。tた、前記細管部8Aには
側管8Bが設けられ、この側管8Bはガスボンがスボン
ベ12には、雰囲気がスとしての空気、酸素、窒素、ア
ンモニア、フレオン等のいずれかのガスが目的に応じて
収容されてお9、例えば、実際に試料が使用される状況
が空気中である場合には空気が用いられ、実際には空気
中で使用される場合でも空気中の酸素による試料の劣化
が問題となる場合等には酸素が使用され、あるいは実際
K11l冷媒の雰囲気下で試料が使用される場合にはア
ンモニアやフレオンが用いられる。ガスボンベ12に収
容され之零吐気ガスは前記側管8Bよりガラス7リンダ
1内に導入された後漏斗2の細管部28を経てガラスシ
リンダ1の外部へと排出されるようになっている。なお
、側管8Bよシ導入される雰囲気ガスは下向きの吹出し
口8Cよシ下向きに吹出され、試料のミストが側管8B
内に入り込まないようになっている。
An Fi funnel-shaped connector 8 is attached to the lower end opening of the glass cylinder 1.
is installed. The upper end edge of this connector 8 is brought into close contact with the lower end edge of the glass cylinder 1 via a sliding part 9 to prevent gas leakage, and the connector 8
The narrow tube part 8A is inserted downward through the center of a lid part 11 made of rubber or the like fitted into the opening of a storage tank 10 shaped like a wide-mouthed bottle, and is connected to the inside of the glass cylinder 1 by the p1 connector 8. It is in communication with the inside of the storage tank 10. In addition, the thin tube portion 8A is provided with a side tube 8B, and the side tube 8B is used to store a gas cylinder, and the gas cylinder 12 is provided with an atmosphere containing any gas such as air, oxygen, nitrogen, ammonia, freon, etc. For example, if the sample is actually used in air, air is used, and even if the sample is actually used in air, the oxygen in the air may Oxygen is used when deterioration is a problem, or ammonia or Freon is used when the sample is actually used in an atmosphere of K11l refrigerant. The zero exhaled gas contained in the gas cylinder 12 is introduced into the glass 7 cylinder 1 through the side pipe 8B, and then is discharged to the outside of the glass cylinder 1 through the narrow tube portion 28 of the funnel 2. Note that the atmospheric gas introduced through the side pipe 8B is blown out downward through the downward outlet 8C, and the sample mist is passed through the side pipe 8B.
It is designed to prevent it from getting inside.

前記、二種10内には、潤滑油、油脂類等の有機化合物
流体である試料13が所定量収容されているとともに、
貯槽10は内部に冷却水等の恒温用流体14が流される
二重壁15t−有する二重壁構造とされ、貯槽10内の
試料13は前記恒温用流体14により所定の温度に維持
されるようKなっている。
A predetermined amount of a sample 13, which is an organic compound fluid such as lubricating oil or fats and oils, is contained in the second type 10, and
The storage tank 10 has a double wall structure with a double wall 15t through which a constant temperature fluid 14 such as cooling water flows, and the sample 13 in the storage tank 10 is maintained at a predetermined temperature by the constant temperature fluid 14. It's K.

貯槽10め底部には、コック16を有するドレイン1T
が設けられており、このドレイン17より試料13が適
宜サンプリングされ得るよう罠なっている。
A drain 1T with a cock 16 is installed at the bottom of the storage tank 10.
is provided, and serves as a trap so that the sample 13 can be sampled from this drain 17 as appropriate.

また、貯槽10内の試料13には吸込管18が差し込ま
れておシ、吸込管18は貯槽10の第1の枝管19にデ
ムー栓20を介しで支持されている。
Further, a suction pipe 18 is inserted into the sample 13 in the storage tank 10, and the suction pipe 18 is supported by a first branch pipe 19 of the storage tank 10 via a Demu plug 20.

吸込管18は貯槽10の外部に配置された循環ボン7”
21に連通され、貯槽10内の試料13は循環ポンプ2
1の作用により吸込管18より吸込された後循環ポンプ
21を経て分岐され、一方は第1の調整弁22を介して
前記蓋部11に貫挿保持された戻し管23よシ再び貯槽
10内に戻され、他方は第2の調整弁24を介して前記
試料導入部5へ送られるよう構成されている。さらに、
貯槽10内には貯槽10の第2の枝管25よシシール部
26を介して撹拌棒27が導入され、撹拌棒27はモー
タ(図示せず)によシ回転されて貯槽10内の試料13
が攪拌されるようになっているとともに、貯槽10内の
試料13内には測定器28がイム栓29を介して前記蓋
部11よシ導入されている。
The suction pipe 18 is a circulation bong 7'' located outside the storage tank 10.
21, and the sample 13 in the storage tank 10 is connected to the circulation pump 2.
After being sucked in from the suction pipe 18 by the action of 1, it is branched through the circulation pump 21, and one side is drawn into the storage tank 10 again through the return pipe 23 inserted and held in the lid part 11 via the first regulating valve 22. and the other is sent to the sample introduction section 5 via the second regulating valve 24. moreover,
A stirring rod 27 is introduced into the storage tank 10 through the second branch pipe 25 of the storage tank 10 and the seal portion 26, and the stirring rod 27 is rotated by a motor (not shown) to stir the sample 13 in the storage tank 10.
At the same time, a measuring device 28 is introduced into the sample 13 in the storage tank 10 through the lid part 11 via a stopper 29.

測定器2Bは透過率自動測定計、吸光率自動測定計、屈
折率自動測定針、粘度自動測定計勢の各SS+定計が適
宜選択されて用いられており、試料130種々の性状変
化が目的に応じて測定され得るようになっている。
Measuring equipment 2B is an automatic transmittance measuring meter, an automatic absorbance measuring meter, an automatic refractive index measuring needle, and an automatic viscosity measuring meter, each of which is selected as appropriate and is used to measure various properties of the sample 130. can be measured accordingly.

次に本発明による評価装置の前記実施例を用いで、潤滑
油等の有機化合物流体を評価する場合について説明する
Next, a case will be described in which an organic compound fluid such as lubricating oil is evaluated using the above embodiment of the evaluation apparatus according to the present invention.

貯槽10内に所定量収容されている試料13を二重壁1
5内に冷却水等の恒温用流体14を流すことに工す、所
定温度、例えば試料13として潤滑油を用いる場合には
30℃〜100℃内の所定温度に維持しながら、撹拌棒
27により貯槽10内を攪拌して貯槽10内の試料13
を均一化する。
A predetermined amount of the sample 13 contained in the storage tank 10 is placed in the double wall 1
A constant temperature fluid 14 such as cooling water is flowed into the chamber 5 at a predetermined temperature, for example, when lubricating oil is used as the sample 13, the temperature is maintained at a predetermined temperature within the range of 30°C to 100°C, using a stirring rod 27. The sample 13 in the storage tank 10 is stirred inside the storage tank 10.
equalize.

ついで、循環ポン7’21を作動させ、且、調整弁22
.24を調整して、貯槽10内の試料13を吸込管18
から吸込ませるとともに、所定の値の一定量の前記試料
13は試料導入部5へと供給され、残りの試料13は戻
し管23より貯槽10内に戻されるように試料13を所
定の循環速度で循環させる。
Next, the circulation pump 7'21 is activated, and the regulating valve 22 is activated.
.. 24 and transfer the sample 13 in the storage tank 10 to the suction pipe 18.
The sample 13 is circulated at a predetermined circulation speed so that a certain amount of the sample 13 with a predetermined value is supplied to the sample introduction section 5 and the remaining sample 13 is returned into the storage tank 10 through the return pipe 23. Circulate.

試料導入部5に供給された試料13Fi、漏斗20円錐
状の大径部2Aの上方部へと流下され友後、大径部2^
の外周面に沿って薄膜化されながら流下され、一様な厚
さの薄膜状となってガラスシリンダ1の内周面1Aへと
伝わっていく。
The sample 13Fi supplied to the sample introduction part 5 flows down to the upper part of the conical large diameter part 2A of the funnel 20, and after that, the large diameter part 2^
It flows down while becoming a thin film along the outer circumferential surface of the glass cylinder 1, and is transmitted to the inner circumferential surface 1A of the glass cylinder 1 in the form of a thin film having a uniform thickness.

内周面1Aに沿って流下する前記試料13は円柱状の一
様な厚さの薄膜[6となって前記内周面1^の長手方向
の略全長に亘って流下されていくが、この際、前記薄膜
部6は加熱器11により所定の温度、例えば試料13が
潤滑油である場合は60℃〜800℃内の所定の温度て
あって前記貯槽10内の試料13の温度よりも高い温度
に加熱されて劣化されるとともに、前記吹出し口8日よ
り吹き出され友のちガラスシリンダ1内を充満しながら
上昇する雰囲気ガスに接触され且触媒30にも接触され
てこれら雰囲気ガスおよび触媒30によシ劣化状態が影
曽されながら流下していく。
The sample 13 flowing down along the inner circumferential surface 1A becomes a cylindrical thin film [6] with a uniform thickness, and flows down almost the entire length of the inner circumferential surface 1^ in the longitudinal direction. At this time, the thin film portion 6 is heated to a predetermined temperature by a heater 11, for example, if the sample 13 is lubricating oil, the predetermined temperature is within 60°C to 800°C, which is higher than the temperature of the sample 13 in the storage tank 10. While being heated to a high temperature and deteriorating, it is also brought into contact with the atmospheric gas that is blown out from the air outlet and rises while filling the inside of the glass cylinder 1, and is also brought into contact with the catalyst 30, so that these atmospheric gases and the catalyst 30 are It flows down the river, showing its deteriorated condition.

ガラスシリンダ10下亀Stで流下した試料13は連結
部8を経て前記貯槽10内へと滴下され、貯槽10内に
戻された試料13は所定の温度まで降温され且攪拌均−
化される。
The sample 13 that has flown down from the lower part of the glass cylinder 10 St is dropped into the storage tank 10 through the connection part 8, and the sample 13 returned to the storage tank 10 is cooled to a predetermined temperature and then stirred and homogenized.
be converted into

このような過程が絶えず繰シ返されるように試料13會
儂璋させながら、前記測定器28により貯槽10内の試
料13の性状変化を測定し、あるいはまた、過電前記ド
レイン17よりサンプリング全行い、全wI価、中和価
、赤外線吸収スペクトル等の各攬スペクトル、ガス分析
等の試験を行うことに り試料13の評価を行う。
While the sample 13 is kept agitating so that such a process is constantly repeated, changes in the properties of the sample 13 in the storage tank 10 are measured by the measuring device 28, or alternatively, all sampling is performed from the over-current drain 17. Sample 13 is evaluated by conducting tests such as total wI value, neutralization value, various spectra such as infrared absorption spectrum, and gas analysis.

このような本実施例によれば次のような効果がある。This embodiment has the following effects.

有機化合物流体である潤滑油等の試料13が、実際に使
用される場合での状況に近似しfc条件下で強制劣化さ
れる次め、試料13t−適正に評価することか可能とな
つ九。
Sample 13, which is an organic compound fluid such as lubricating oil, is forcibly degraded under FC conditions that approximate the conditions in which it is actually used, and then it becomes possible to properly evaluate sample 13t.

例えば、以下に掲げる第1表には試料として2種の潤滑
油A、B(ともに酸化防止剤としてZnDTPが含まれ
ている。)を用いて本実施例による評価結果およびロー
タリボンデ酸化安定度試験による評価結果が実機での実
際の寿命との比較において示されている。ここにおいて
、本実施例における評価結果として採用されている時間
は各試料の全酸価が最低となるまでの時間であシ、この
時間を寿命とするのは、酸化防止剤として添加されてい
るZn DTPが酸化されるに従い分解し、全部分解し
てしまうと酸化防止能が無くなり全酸価が上昇しはじめ
ることに着目し、ZnDTPが全部分解する壕での時間
を潤滑油の寿命とすべきだからである。なお、酸化防止
剤を含まない潤滑油にあっては測定直後から全酸価が上
昇し、この場合は全酸価が一定値(例えば0.5)にな
るまでの時間を寿命とすればよい。
For example, Table 1 listed below shows the evaluation results and rotary ribbon oxidation stability test according to this example using two types of lubricating oils A and B (both containing ZnDTP as an antioxidant) as samples. The evaluation results are shown in comparison with the actual lifespan of an actual machine. Here, the time adopted as the evaluation result in this example is the time until the total acid value of each sample reaches its minimum, and this time is defined as the life of the sample added as an antioxidant. Focusing on the fact that ZnDTP decomposes as it is oxidized, and once it is completely decomposed, the oxidation prevention ability is lost and the total acid value begins to rise, the lifespan of the lubricant should be defined as the time in the trench where ZnDTP is completely decomposed. That's why. In addition, for lubricating oils that do not contain antioxidants, the total acid value increases immediately after measurement, and in this case, the time until the total acid value reaches a constant value (for example, 0.5) can be defined as the life span. .

第   1   表 1111’j!機テノ寿命”’ぺ 7ボンプ(V−10
4C111)を用いた油圧システムに油温65℃と いう潤滑条件下で略連続的に使用し友。
1st table 1111'j! Machine life span "'pe 7bonp (V-10
It can be used almost continuously in a hydraulic system using 4C111) under lubricated conditions with an oil temperature of 65℃.

12本実施例゛°・試料としての潤滑油全量:300’
−を循環速度;1.1wLV分 加熱温度;300℃ 貯槽温度;140℃ 雰囲気がス1空気(flt量 5L膚)触媒寡全長3慣
、直径1.6−の銅コイル※30−タリボンプ酸化安定
度試験・・・ASTM D 2272に準拠した。
12 Examples゛°・Total amount of lubricating oil as sample: 300'
- Circulation rate: 1.1wLV min Heating temperature: 300℃ Storage tank temperature: 140℃ Atmosphere is 1 air (flt amount 5L), catalyst is small, overall length is 3, diameter is 1.6mm Copper coil *30 - Talibump oxidation stable Degree test: Based on ASTM D 2272.

第1表からも明らからように、ロータリボンデ酸化安定
度試験では実機での潤滑油の寿命を推定することが不可
能であるが、本実施例によれば本機での潤滑油の寿命を
極めて正確に推定することが可能である。
As is clear from Table 1, it is impossible to estimate the life of the lubricating oil in the actual machine using the rotary ribbon oxidation stability test, but according to this example, the life of the lubricating oil in the machine can be estimated. It is possible to estimate it very accurately.

また、本実施例によれば、試料13が薄−膜状にて加熱
され且雰囲気がスや触媒30に接触されるものである几
め強制劣化が短時間で進行され、し九がって試料13金
迅速に評価することが可能となる。
Further, according to this embodiment, the sample 13 is heated in the form of a thin film and brought into contact with the atmosphere and the catalyst 30, so that the forced deterioration progresses in a short period of time. It becomes possible to quickly evaluate sample 13 gold.

例えば、以下に掲げる第2表には試料として3種の潤滑
油C,D、 E (すべて酸化防止剤としてのZn D
TPが含まれている。)t−用いて本実施例による評価
結果およびインディアナ酸化試験による評価結果が比較
して示されている。ここにおいて、評価結果として採用
されている時間1ユ各試料の全酸価が最低となるまでの
時間である。
For example, Table 2 below lists three types of lubricating oils C, D, and E (all containing Zn D as an antioxidant) as samples.
Contains TP. ) The evaluation results according to this example and the evaluation results according to the Indiana oxidation test are shown for comparison. Here, the time adopted as the evaluation result is the time until the total acid value of each sample reaches its minimum.

第   2   表 秦4本実施例・・・加熱温度全280℃とし九以外は前
出のJIII表における条件と同様の条件とし九〇 ※5 インディアナ酸化試験・・・反応温度を140t
:とじて、スタンダードオイル−インディ アナ社の提案する方法に準拠し九。
Table 2 Hata 4 This example: The heating temperature was 280°C in total, and the conditions were the same as those in Table JIII above, except for 9. *5 Indiana oxidation test: The reaction temperature was 140 t.
: According to the method proposed by Standard Oil-Indiana Company.

第2表からも明らかなように、本実施例によればインデ
ィアナ酸化試験との間に相関関係があり、しかも、所要
時間は手分程度の短時間で済むものである。
As is clear from Table 2, according to this example, there is a correlation with the Indiana oxidation test, and the time required is only about a minute.

なお、上述の実施例では、ガラスシリンダ1と貯槽10
とは別々に構成されているものとしたが、一体屹6るい
は連続的に構成されていてもよい。
In addition, in the above-mentioned embodiment, the glass cylinder 1 and the storage tank 10
Although it is assumed that they are configured separately from each other, they may be configured integrally or continuously.

また、試″N13が薄膜状となって流下される壁面は、
鉛直に配置されたガラスシリンダ1の内周面1Aよりな
るものとしたが、第2図に示される他の実施例のように
、前記壁面は平板面状の加熱プレート51の上趨面51
Aよりなり且上端面51Aが所定の角度に傾斜されてい
るようなものであってもよい。すなわち、第2図に示さ
れる他の実施例では、前記加熱グレー1−51Fi、所
定の角度に傾斜されて配置され且図中上下方向より偏平
化された略長方体状のがラスチャンバ52の下方側の側
壁よりなり、前記側壁には加熱機構Tが併設されている
。また、ガラスチャンバ52内に:はガス導入口53よ
り雰囲気ガスが導入され、この雰囲気ガスはガラ、スチ
ャンバ52内を充満した後がス導出口54より導出され
るようになっている。
In addition, the wall surface on which the sample N13 flows down in a thin film form is
Although the inner circumferential surface 1A of the glass cylinder 1 is arranged vertically, as in the other embodiment shown in FIG.
A, and the upper end surface 51A may be inclined at a predetermined angle. That is, in the other embodiment shown in FIG. 2, the heating gray 1-51Fi is a substantially rectangular rectangular parallelepiped that is inclined at a predetermined angle and is flattened in the vertical direction in the figure. It consists of a lower side wall, and a heating mechanism T is attached to the side wall. Further, an atmospheric gas is introduced into the glass chamber 52 through a gas inlet 53, and after the atmospheric gas fills the glass chamber 52, it is led out through a gas outlet 54.

前記カラスチャンバ52の上趨側には流下ノズル55が
取付けられており、この流下ノズル55の失地側は、第
3図に示されるように、狭幅なスリット出口55Aを有
するよう偏平化されてお9、流下ノズル55よシ前記上
端面51A上に流下される試料13は上端面51A上に
で薄膜化されるようKなっている。また、ガラスチャン
バ52の下11111[には細管状の滴下部56が一体
的に形成されておシ、前記上端面51A上を薄膜状の薄
膜部6となって流下された試料13は滴下部561−経
て貯槽10へと流入するよう罠なっている。なお、前記
加熱!レート51および流下ノズル55より薄膜発生機
構57が構成されている。
A downstream nozzle 55 is attached to the upper side of the crow chamber 52, and the losing side of the downstream nozzle 55 is flattened to have a narrow slit outlet 55A, as shown in FIG. 9. The sample 13 that is flown down onto the upper end surface 51A from the flow nozzle 55 is formed into a thin film on the upper end surface 51A. In addition, a thin tube-shaped dripping portion 56 is integrally formed at the bottom 11111 of the glass chamber 52, and the sample 13 that has flown down as a thin film portion 6 on the upper end surface 51A is transferred to the dripping portion. 561- and into the storage tank 10. In addition, the heating mentioned above! The rate 51 and the downstream nozzle 55 constitute a thin film generating mechanism 57.

このような第2、図に示される実施装置によれば、試料
13が極めて粘度の低いものである場合にも比較的長時
間薄膜状にさせておくことができる。
According to the second embodiment shown in the figure, even when the sample 13 has an extremely low viscosity, it can be kept in a thin film form for a relatively long period of time.

さらにまた、試料13が薄膜状となって流下される1I
IWJは、円柱体や円錐体等、の外周面形状などであっ
てもよい。
Furthermore, the sample 13 flows down in the form of a thin film.
The IWJ may have an outer peripheral surface shape such as a cylinder or a cone.

また、薄膜状とされ九試料13には、雰囲気ガスや触媒
30が接触されるものとし友が、評価の目的に、−じて
は、これらの一方あるいは双方が接触されないものであ
ってもよい。
Furthermore, although the sample 13, which is in the form of a thin film, is supposed to be brought into contact with the atmospheric gas and the catalyst 30, for the purpose of evaluation, one or both of these may not be brought into contact. .

また、雰囲気がスは連続的に流されるものとし皮が、ガ
ラスシリンダ1やがラスチャンバ52内に所定圧の雰囲
気ガスが封入されていてもよく、この場合には封入され
た雰囲気ガスの圧力降下を測定して試料13の寿命を評
価してもよい。
Further, the atmosphere is assumed to be continuously flowed, and an atmospheric gas at a predetermined pressure may be sealed in the glass cylinder 1 or the glass cylinder 52, and in this case, the pressure of the sealed atmospheric gas will drop. The life of the sample 13 may be evaluated by measuring.

上述のように、本発明によれば有機化合物流体を適正且
迅速に評価することのできる有機化合物流体の評価方法
および評価装置を提供することができる。
As described above, according to the present invention, it is possible to provide an organic compound fluid evaluation method and an evaluation apparatus that can appropriately and quickly evaluate an organic compound fluid.

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

第1図は本発明に係る有機化合物流体の評価装置の一実
施例の全体構成を示す断面図、第2図は他の実施例の要
部を示す断面図、第3図は第2図に示され曳実施1例に
おける流下ノズルの形状を示す拡大斜視図である。 1°・・ガラスシリンダ、IA、51・A・・・有機化
合物流体が流下される壁面としての9内周面、上端面、
2・・・漏斗、3,57・・・薄膜発生機構、6・・・
薄膜部、7・・・加熱機構、10・・・貯槽、13°・
・有機化合物流体である試料、14・・・・恒温用流体
、12・・・ガスボンベ、21・・・循環ポンプ、51
・・・加熱プレート、55・・・流下ノズル。 代理人 弁理士 木 下 實 三
FIG. 1 is a sectional view showing the overall configuration of one embodiment of the organic compound fluid evaluation device according to the present invention, FIG. 2 is a sectional view showing the main parts of another embodiment, and FIG. 3 is similar to FIG. FIG. 2 is an enlarged perspective view showing the shape of a downstream nozzle in one example of the towing embodiment shown in FIG. 1°...Glass cylinder, IA, 51.A...9 inner peripheral surface as a wall surface on which the organic compound fluid flows down, upper end surface,
2... Funnel, 3,57... Thin film generation mechanism, 6...
Thin film part, 7... Heating mechanism, 10... Storage tank, 13°.
- Sample that is an organic compound fluid, 14... Constant temperature fluid, 12... Gas cylinder, 21... Circulation pump, 51
... Heating plate, 55... Downstream nozzle. Agent Patent Attorney Minoru Kinoshita

Claims (1)

【特許請求の範囲】 (1)  試料としての有機化合物流体を強制劣化させ
てその劣化度を測定することによフ有機化合物流体を評
価する有機化合物流体の評価方法において、前記試料の
一部を薄膜状にした後に一旦貯槽内に導入する一方で貯
槽内の試料の一部を取出して薄膜状にするより試料を循
環させながら、主として薄膜状の試料の劣化を促進させ
る仁とにょ9試料量体を強制劣化させることを特徴とす
る有機化合物流体の評価方法。 (2)特許請求の範S第1項において、前記薄膜状にし
友試料を加熱するとともに1貯槽内においては前記加熱
された試料を降温させることt特徴とする有機化合物流
体の評価方法。 (糾 特許請求の範囲第1項又は第2項において、前記
薄膜状にした試料に雰−気ガスを接触させることを特徴
とする有機化合’IIR体の評価方法。 (4)試料としての有機化合物流体が薄膜状となって流
下される傾けられ若しくは鉛直方向に向けられた壁面を
備えた薄膜発生機構と、前記壁面の下方側に配置され流
下された試料を収容する貯槽と、貯槽内の試料を前記薄
膜発生機構に供給する循環ポンプとを有すること′f:
%徴とする有機化合物流体の評価装置。
[Claims] (1) In an organic compound fluid evaluation method for evaluating an organic compound fluid by forcibly degrading the organic compound fluid as a sample and measuring the degree of deterioration, a part of the sample is After making it into a thin film, it is first introduced into the storage tank, and then a part of the sample in the storage tank is taken out and made into a thin film.While the sample is being circulated, the amount of sample is mainly accelerated, which accelerates the deterioration of the thin film sample. A method for evaluating organic compound fluids characterized by forced deterioration of the body. (2) A method for evaluating an organic compound fluid according to claim S, characterized in that the sample formed into a thin film is heated and the heated sample is cooled in one storage tank. (Conclusion) A method for evaluating an organic compound 'IIR compound according to claim 1 or 2, characterized in that the thin film sample is brought into contact with an atmospheric gas. (4) An organic compound as a sample a thin film generation mechanism having an inclined or vertically oriented wall surface through which the compound fluid flows down in the form of a thin film; a storage tank disposed below the wall surface for accommodating the sample that has flown down; and a circulation pump for supplying the sample to the thin film generation mechanism'f:
Evaluation device for organic compound fluids based on % characteristics.
JP4600582A 1982-03-23 1982-03-23 Method and apparatus for estimating organic compound fluid Granted JPS58162865A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4600582A JPS58162865A (en) 1982-03-23 1982-03-23 Method and apparatus for estimating organic compound fluid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4600582A JPS58162865A (en) 1982-03-23 1982-03-23 Method and apparatus for estimating organic compound fluid

Publications (2)

Publication Number Publication Date
JPS58162865A true JPS58162865A (en) 1983-09-27
JPS6412341B2 JPS6412341B2 (en) 1989-02-28

Family

ID=12734949

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4600582A Granted JPS58162865A (en) 1982-03-23 1982-03-23 Method and apparatus for estimating organic compound fluid

Country Status (1)

Country Link
JP (1) JPS58162865A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6365413B1 (en) * 1998-02-27 2002-04-02 Savant, Inc. Thin film thermal oxidative oil deposit testing device and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6365413B1 (en) * 1998-02-27 2002-04-02 Savant, Inc. Thin film thermal oxidative oil deposit testing device and method

Also Published As

Publication number Publication date
JPS6412341B2 (en) 1989-02-28

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