JPS62180711A - Deaerator - Google Patents
DeaeratorInfo
- Publication number
- JPS62180711A JPS62180711A JP2195086A JP2195086A JPS62180711A JP S62180711 A JPS62180711 A JP S62180711A JP 2195086 A JP2195086 A JP 2195086A JP 2195086 A JP2195086 A JP 2195086A JP S62180711 A JPS62180711 A JP S62180711A
- Authority
- JP
- Japan
- Prior art keywords
- flow path
- path pipe
- tube
- tank
- deaerated
- 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.)
- Pending
Links
- 239000007788 liquid Substances 0.000 claims abstract description 10
- 230000035699 permeability Effects 0.000 claims abstract description 9
- 239000000126 substance Substances 0.000 claims abstract description 5
- 238000007872 degassing Methods 0.000 claims description 17
- 238000004804 winding Methods 0.000 abstract description 2
- 230000002093 peripheral effect Effects 0.000 abstract 1
- 238000004513 sizing Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 7
- 239000003153 chemical reaction reagent Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 125000006850 spacer group Chemical group 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 229910001369 Brass Inorganic materials 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 235000012489 doughnuts Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000003014 reinforcing effect Effects 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0031—Degasification of liquids by filtration
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Degasification And Air Bubble Elimination (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕 :
本発明は、生化学自動分析装置もしくは液体クロマトグ
ラフ等の脱気装置の改良に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application]: The present invention relates to improvement of a degassing device such as an automatic biochemical analyzer or a liquid chromatograph.
一般に、生化学自動分析装置において、試薬中に溶存し
ている空気は温度変化等で流路管中で発泡し、それが特
に試薬分注装置近辺で滞留すると、非圧縮性流体が圧縮
性流体と化し、容積形分注装置の容積が変動し量の正確
性が低下する。また、液体クロマトグラフにおいては、
流路中で発泡した空気によシ定常流が得られなくなシ検
出誤差を致命的に増大させることになる。従来このため
に、特開昭51−28261号公報、特開昭54−12
3785号公報、特開昭57−165007号公報が提
案されている。In general, in automatic biochemical analyzers, air dissolved in reagents foams in the flow pipe due to temperature changes, etc., and when it stagnates especially near the reagent dispensing device, incompressible fluid becomes compressible fluid. As a result, the volume of the positive displacement dispensing device fluctuates, reducing the accuracy of the amount. In addition, in liquid chromatography,
The air bubbled in the flow path makes it impossible to obtain a steady flow, which will fatally increase detection errors. Conventionally, for this purpose, Japanese Patent Application Laid-Open No. 51-28261, Japanese Patent Application Laid-Open No. 54-12
No. 3785 and Japanese Unexamined Patent Publication No. 165007/1987 have been proposed.
しかし、いかに気体透過性がすぐれた材質を用いて流路
管を形成しても、現在知られているガス透過性では、必
要な脱気量を得るためには流路管長が長大になることは
避けられない。このため、特開昭51−28261号公
報では、流路の出入口を、分岐状構造にし、流路管を2
以上並列にして問題□を解決している。また、特開昭5
4−123785、特開昭57−165007号公報で
は、流路管をンレノイドコイル状に巻いて問題を解決し
ている。と午ろで、流路出入口を分岐状構造にすること
は長尺の場合でも勿論同様であるが、生化学自動分析装
置の試薬などのように劣化が短時日で起こシ、かつ、高
価なものの被脱気液を新鮮なものと置換する際に、微小
量の試薬を迅速に置換することが困難になる。即ち、分
岐部構造部分に交換を要する試薬がたまシ易い。また、
流路管をンレノイドコイル状に巻いた構造においては、
スペースの関係上軸方向に管どうしが近接し接触する場
合があり脱気効率が悪い。However, no matter how highly gas permeable a material is used to form the flow path, the currently known gas permeability means that the length of the flow path will be long in order to obtain the required amount of deaeration. is unavoidable. For this reason, in Japanese Patent Application Laid-Open No. 51-28261, the entrance and exit of the flow path is made into a branched structure, and the flow path pipe is divided into two.
Problem □ is solved by parallelizing the above. Also, JP-A-5
No. 4-123785 and Japanese Unexamined Patent Application Publication No. 57-165007 solve the problem by winding the flow pipe into a coil shape. Of course, creating a branched structure at the inlet and outlet of the flow channel is the same even when the channel is long, but it is difficult to use a reagent for an automatic biochemical analyzer that deteriorates in a short period of time and is expensive. When replacing the liquid to be degassed with a fresh one, it becomes difficult to quickly replace a small amount of reagent. That is, reagents that need to be replaced are likely to accumulate in the branch structure. Also,
In the structure where the flow pipe is wound into a renoid coil,
Due to space constraints, the pipes may come close to each other in the axial direction and come into contact with each other, resulting in poor deaeration efficiency.
上記従来の構造においては、所定量の脱気量を得ようと
するためには流路管長を長大に要し、このため流路管を
コイルばね状に形成したシ、出入口部分に分岐部構造を
設けて並列にしたシしているが、構造が大きく脱気効率
が低く取扱い性が悪い等の問題点があった。このため、
本発明は流路管の配置及び支持構造を改善し、隣接管ど
うしが所定の間隔を保持し接触しないように渦巻き平面
状に支持し、隣接管どうしが接しないことによシ管外周
全面によシ脱気され脱気量を増大することができ、簡単
な構造で、装置を小形化し効率よく脱気ができる脱気装
置を提供することを目的としたものである。In the above-mentioned conventional structure, in order to obtain a predetermined amount of deaeration, a long flow path tube is required. However, there were problems such as the large structure, low degassing efficiency, and poor handling. For this reason,
The present invention improves the arrangement and support structure of flow path pipes, and supports them in a spiral plane so that adjacent pipes maintain a predetermined interval and do not come into contact with each other. The object of the present invention is to provide a degassing device which can perform good degassing and increase the amount of degassing, has a simple structure, is miniaturized, and can perform degassing efficiently.
上記問題点を解決するために本発明においては。 In order to solve the above-mentioned problems, the present invention aims to solve the above problems.
気体透過性が良好で、かつ、耐薬品性にすぐれ内部に被
脱気液が流動される可撓性流路管と、該流路管を収蔵す
ると共に該流路管の外側である内部が真空排気されるよ
うに形成されている脱気タンクとを設けてなシ、上記流
路管が、隣接円外周管との間を所定の間隔に保ちほぼ渦
巻き平面状に少なくとも1層に保持し形成されているも
のである。A flexible channel tube that has good gas permeability and excellent chemical resistance and allows the liquid to be degassed to flow inside, and an interior that houses the channel tube and is the outside of the channel tube. A deaeration tank formed to be evacuated is not provided, and the flow path pipe is maintained in at least one layer in a substantially spiral planar shape with a predetermined distance between the adjacent circular outer circumferential pipes. It is being formed.
流路管19は、はぼ渦巻き状で平板状に形成さねておシ
、隣接円外周管との間が近接または接触することなく所
定の距離が保たれていることによシ、流路管19内の被
脱気液は脱気タンク20内の真空雰囲気内で効率よ〈脱
気作用が行なわれる。The flow path pipe 19 is not formed into a spiral shape and a flat plate shape, but is maintained at a predetermined distance from adjacent circular outer circumferential tubes without being close to each other or in contact with each other. The liquid to be degassed in the pipe 19 is efficiently degassed in the vacuum atmosphere in the deaeration tank 20.
また、流路管19が金網1a、lbの溝28中に収容さ
れることによシ流路管壁を薄く形成することができ流路
管19の材質が溶解拡散型の均質膜の場合について述べ
ると、流路管19中の被脱気液中の溶存空気(ffi単
のため、に酸素で代表する)が単位時間(t)K’1i
iF壁を透過する量(cr)は(1)式で表される。Furthermore, since the channel tube 19 is housed in the groove 28 of the wire meshes 1a and 1b, the channel tube wall can be formed thinly, and the material of the channel tube 19 is a dissolution-diffusion type homogeneous membrane. In other words, the dissolved air (represented by oxygen because it is simply ffi) in the liquid to be degassed in the flow path pipe 19 per unit time (t) K'1i
The amount (cr) transmitted through the iF wall is expressed by equation (1).
但し、K::酸素の透過係数
ΔP:流路管内外の酸素の平均分圧差
S:流路管の肉厚
′ dで流路管の相当直径
t□:流路管の長さ :
A:気体透過rrJ積 ・
本発明では流路管19の外壁を相互に接することかない
空間に配設することにょシ、気体透過面積人を2πd/
、に等しくなるように(理論値と同じになるように)に
なシ脱気が全面からなされ、さらK、流路管19の外周
を補強す□ることにょシ流路管19の肉厚Sを薄くでき
酸素の透過性を改善できる。However, K:: Oxygen permeability coefficient ΔP: Average partial pressure difference of oxygen inside and outside the flow pipe S: Wall thickness of the flow pipe ′ d and equivalent diameter of the flow pipe t□: Length of the flow pipe: A: Gas permeation rrJ product - In the present invention, since the outer walls of the flow path pipes 19 are arranged in spaces that do not touch each other, the gas permeation area is 2πd/
Deaeration is performed from the entire surface so that it is equal to (same as the theoretical value), and the wall thickness of the flow path tube 19 is further reinforced by reinforcing the outer periphery of the flow path tube 19. S can be thinned and oxygen permeability can be improved.
〔実施例〕□□
以下本発明の脱気装置を実施例を用い第1図に□よ#)
説明する。第1図は脱気タンクのみを断面で示した説明
歯である。図においてs 1. I’a、 11は金
網、2a、2bは入口、3a、3bは出口。[Example] □□ Hereinafter, the deaerator of the present invention will be shown in Fig. 1 using an example.
explain. FIG. 1 is an explanatory diagram showing only the deaeration tank in cross section. In the figure s1. I'a, 11 is a wire mesh, 2a, 2b are entrances, 3a, 3b are exits.
4はスペーサ、5は軸、6.7は鏡板、8は筒、、10
は0リノグ、11はねじである。また。4 is a spacer, 5 is a shaft, 6.7 is an end plate, 8 is a cylinder, 10
is 0 linog and 11 is screw. Also.
12は排気口1.13は真空ポンプ、14は真空ポンプ
駆動用のモータ、15は真空スイッチ、16はコントロ
→う、20は脱気タンクである。金網1は平面図を第2
図に示し、一部の断面図を第3囚に示すようにほぼ渦巻
き状(アルキメデスのスパイラル形状を含む)の溝28
を有する平面形状に形成され溝28内に第3図に示すよ
うに流路管19が挿入され流路管19は変位を阻止され
ている。流路管19は気体透過性が良好で、かつ、耐薬
品性がすぐれ可撓性を有し、内部に被脱気液が流動され
るようになっている。!4図は第1図の金網部と同部分
の断面説明口であシ、第4@の構造の場合は2流路分対
向しておシ金網1a、lbはスペーサ4で隔離されてい
る。入口2a、2b出口3a、3bは筒8を気密に貫通
固定されている。金網1a、lb及びスベーf’4は中
心部を貫通する軸5に固定さね、軸5は鏡板6,7によ
り筒8に同心的にねじIIKよって固定されており。12 is an exhaust port 1, 13 is a vacuum pump, 14 is a motor for driving the vacuum pump, 15 is a vacuum switch, 16 is a control, and 20 is a degassing tank. Wire mesh 1 has a plan view as 2nd
As shown in the figure and a partial cross-sectional view shown in the third figure, the groove 28 has a substantially spiral shape (including an Archimedean spiral shape).
As shown in FIG. 3, the channel tube 19 is inserted into the groove 28, and the channel tube 19 is prevented from being displaced. The flow path pipe 19 has good gas permeability, excellent chemical resistance, and flexibility, and allows the liquid to be degassed to flow inside. ! 4 is a cross-sectional explanatory opening of the same part as the wire mesh portion in FIG. The inlets 2a, 2b and the outlets 3a, 3b are hermetically fixed through the tube 8. The wire meshes 1a, lb and the base f'4 are fixed to a shaft 5 passing through the center, and the shaft 5 is fixed concentrically to the cylinder 8 by screws IIK between end plates 6 and 7.
これらの接合部は017ング9,10によって気密に保
持されている。These joints are held airtight by 017 rings 9 and 10.
鋼板7には排気口12が開口され、鋼板6.7及び筒8
により脱気タンク20が形成され、脱気タンク20の内
部は真空ボ/プ13.真空スイッチ15に連通され、真
空スイッチ15は脱気タンク20内が所定の真空度にな
ると作用しコントローラエ6を介し真空ポツプ13駆動
用のモータ14を駆動または停止させるようKなってい
る。金網la、lbは同円周30、外円周31、溝28
形成による山29を有し、真鍮またはステンレススチー
ル製の平織金網で形成され、線径が、35または368
WGのものを平織りすると、40または50メツシュ程
度に形成さhて望ましいが、これは後述する溝28の幅
によシ異なる。金網1a。An exhaust port 12 is opened in the steel plate 7, and the steel plate 6.7 and the cylinder 8
A degassing tank 20 is formed by the vacuum tank 13. The vacuum switch 15 is connected to a vacuum switch 15, and the vacuum switch 15 is activated when the inside of the degassing tank 20 reaches a predetermined degree of vacuum to drive or stop the motor 14 for driving the vacuum pop 13 via the controller 6. Wire mesh la and lb have the same circumference 30, outer circumference 31, and groove 28
It has ridges 29 formed by forming, is made of plain weave wire mesh made of brass or stainless steel, and has a wire diameter of 35 or 368.
When a WG material is plain woven, it is desirable to form it with about 40 or 50 meshes, but this varies depending on the width of the grooves 28, which will be described later. Wire mesh 1a.
1bには始端18からアルキメデスのスパイラル状に@
28が形成され終端17で終っている。In 1b, there is an Archimedean spiral @ from the starting point 18.
28 is formed and terminates at the terminal end 17.
溝28の寸法は流路管19の外径と同じかやや大きい程
度で、山29の高さは溝28に流路管19を挿入したと
きの流路管19の高さとほぼ同じ程度が好ましい。上記
程度の寸法の金N41a、lbの場合の流路管19の外
径は3鳩、このときの山29の幅は約1+oである。ま
た、第4図のように金tI41a、lbが同方向に1ね
られた場合はスペーサ4を配設することが望ましいが、
$1図のように対向させたときはスペーサ4を省略でき
る。The dimensions of the groove 28 are preferably the same as or slightly larger than the outer diameter of the flow pipe 19, and the height of the crest 29 is preferably approximately the same as the height of the flow pipe 19 when the flow pipe 19 is inserted into the groove 28. . In the case of gold N41a, lb having the above-mentioned dimensions, the outer diameter of the channel pipe 19 is 3cm, and the width of the ridge 29 in this case is about 1+o. Furthermore, if the gold tI41a and lb are twisted in the same direction as shown in FIG. 4, it is desirable to provide a spacer 4.
$1 When facing each other as shown in the figure, the spacer 4 can be omitted.
また、第1図のように2F−に重ねられた流路管19の
場合1図示のようにそれぞれ独立の流路を形成してもよ
いが、上段、下段の出口どうし、入口どうし、または出
口と入口とを接続して1流路としてもよい。In addition, in the case of the flow path pipes 19 stacked on 2F- as shown in FIG. 1, independent flow paths may be formed as shown in FIG. and the inlet may be connected to form one flow path.
このように本実施例の脱気装置は、気体透過性が良好で
、かつ、耐薬品性にすぐれ内部に被脱気液が流動される
可動性流路管全脱気タンク同に、隣接する同外周管との
間を所定の間隔に保ちほぼ渦巻き平面状に2層に保持形
成したので、流路管外同相互が接することなく多量の脱
気が迅速に円滑に行われ、従って、その分流路管の長さ
を縮少できると共に流路管中に滞留する分を少なくし、
また、簡単な構造で装置を小形化でき、さらに。As described above, the deaeration device of this embodiment has good gas permeability and excellent chemical resistance, and has a movable flow path tube in which the liquid to be degassed flows, and an adjacent deaeration tank. Since the space between the outer circumferential tube and the outer tube is maintained at a predetermined interval and the two layers are formed in an almost spiral planar shape, a large amount of air can be removed quickly and smoothly without the outer circumferential tube coming into contact with each other. The length of the branch pipe can be reduced, and the amount of water remaining in the pipe can be reduced.
In addition, the simple structure allows the device to be made smaller.
流路管は金網に保持され変形を阻止されているので、管
壁を薄くすることができることによシ、よシ効率的に脱
気ができ流路管の長さを短縮できる。Since the channel tube is held by a wire mesh to prevent deformation, the tube wall can be made thinner, and air can be removed more efficiently and the length of the channel tube can be shortened.
第5図、第6図は他の実施例を示し第5図は第21W(
D41M4hZ*f)@*F、fat−;M”JmF)
”F−mG、□6図は第5図の円板に流路管が保持され
友状態の一部の断面図である。本実施例の上記実施例と
異なるところは、流路管19をほぼ渦巻き平面状に保持
するのに、上記実施例はほぼ渦巻き状の溝28を有する
金網1により行なっているのに対し1本実施例は円板上
に突設された複数本のビンによシ保持している点である
。図において、円板21は外円823内円周24を有す
るドーナツ状で、多数の通気孔25と通気1W26を有
し1.円板21上には多数のビン22が所定の角轡で放
射状に所定の間隔で植立されている。そして1.隣接す
るビン22間に流路管19を挿入すると、アルキメデス
のスパイラル状に巻くことができるようになっている。5 and 6 show other embodiments, and FIG. 5 shows the 21W (
D41M4hZ*f) @*F, fat-;M"JmF)
"F-mG," □Figure 6 is a cross-sectional view of a part of the flow path tube in a friendly state where the disk in FIG. While the above embodiment uses the wire mesh 1 having substantially spiral grooves 28 to maintain the substantially spiral plane shape, this embodiment uses a plurality of bottles protruding from the disk. In the figure, the disk 21 has a donut shape with an outer circle 823 and an inner circumference 24, and has many ventilation holes 25 and ventilation holes 1W26. The bottles 22 are arranged radially at a predetermined interval in a predetermined square.When a channel pipe 19 is inserted between adjacent bottles 22, it becomes possible to wind the bottles in an Archimedean spiral shape. There is.
そして、第6図に示すスペーサ27を流路W19の上部
に間隔を置いて−thてもよい。本実施例も上記実施例
と同様の作用効果を有する。Then, a spacer 27 shown in FIG. 6 may be placed at an interval -th above the flow path W19. This example also has the same effects as the above example.
以上記述した如く本発明の脱気装置は、効率よく脱気が
できると共に簡単な構造で装置を小形化できる効果を有
するものである。As described above, the degassing device of the present invention has the effect of efficiently degassing and making the device compact with a simple structure.
第1図は本発明の脱気装置の実施例の脱気タンクを断面
で示した説明口、第2図は第1図のように用いる金網の
平面図、第3図は第2図に流路管が挿入された状態の一
部の断面図、第4図は、!1図の金網部と同部分の一部
の断面図、第5図は本発明の脱気装置の・鴎の実施例の
第1図の金網と同様の機能を有する円板の平面図、第6
図は@5図の円板に流路管を保持させた状態の一部の断
■図である。
1、la、It)・・・金網、13・・・真空ポツプ、
19・・・流路管、20・・・脱気夕/り、21・・・
円板、22・・・ピン、28・・・溝。Figure 1 is a cross-sectional view of a degassing tank of an embodiment of the degassing device of the present invention, Figure 2 is a plan view of a wire mesh used as shown in Figure 1, and Figure 3 is similar to Figure 2. A cross-sectional view of a portion of the pipe with the pipe inserted, Figure 4 is! FIG. 5 is a cross-sectional view of a part of the same part as the wire mesh part in FIG. 1, FIG. 5 is a plan view of a disk having the same function as the wire mesh in FIG. 6
The figure is a partial cross-sectional view of the state in which the flow pipe is held by the disc shown in Figure @5. 1, la, It)...Wire mesh, 13...Vacuum pot,
19... Flow pipe, 20... Deaeration pipe, 21...
Disc, 22...pin, 28...groove.
Claims (1)
に被脱気液が流動される可撓性流路管と該流路管を収蔵
すると共に該流路管の外側である内部が真空排気される
ように形成されている脱気タンクとを設けたものにおい
て、上記流路管が、隣接円外周管との間を所定の間隔に
保ちほぼ渦巻き平面状に少なくとも1層に保持し形成さ
れていることを特徴とする脱気装置。 2、上記流路管が、金網にほぼ渦巻き状に形成された溝
内に保持されている特許請求の範囲第1項記載の脱気装
置。 3、上記流路管が、円板上に突設された複数本のピンに
よりほぼ渦巻き形状を保持するように位置を固定し形成
されている特許請求の範囲第1項記載の脱気装置。[Scope of Claims] 1. A flexible channel tube that has good gas permeability and excellent chemical resistance and allows a liquid to be degassed to flow therein, and a flexible channel tube that houses the channel tube and the channel. A degassing tank is formed so that the inside, which is the outside of the tube, is evacuated, and the flow path tube has a substantially spiral planar shape while maintaining a predetermined distance between the adjacent circular outer circumferential tubes. A deaeration device characterized in that the degassing device is formed by retaining at least one layer of. 2. The degassing device according to claim 1, wherein the flow path pipe is held in a groove formed in a substantially spiral shape in a wire mesh. 3. The degassing device according to claim 1, wherein the flow path pipe is fixed in position by a plurality of pins protruding from a disk so as to maintain a substantially spiral shape.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2195086A JPS62180711A (en) | 1986-02-05 | 1986-02-05 | Deaerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2195086A JPS62180711A (en) | 1986-02-05 | 1986-02-05 | Deaerator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62180711A true JPS62180711A (en) | 1987-08-08 |
Family
ID=12069342
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2195086A Pending JPS62180711A (en) | 1986-02-05 | 1986-02-05 | Deaerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62180711A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0252005A (en) * | 1988-08-12 | 1990-02-21 | Japan Gore Tex Inc | Deaeration mechanism |
JPH0534139A (en) * | 1991-07-30 | 1993-02-09 | Nissan Motor Co Ltd | Measuring apparatus of abrasion of free rail of conveyor |
JPH11137907A (en) * | 1997-11-11 | 1999-05-25 | Moore Kk | Deaerator |
JP2008249508A (en) * | 2007-03-30 | 2008-10-16 | Nakanishi Metal Works Co Ltd | Wear inspection apparatus of conveyor rail |
-
1986
- 1986-02-05 JP JP2195086A patent/JPS62180711A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0252005A (en) * | 1988-08-12 | 1990-02-21 | Japan Gore Tex Inc | Deaeration mechanism |
JPH0534139A (en) * | 1991-07-30 | 1993-02-09 | Nissan Motor Co Ltd | Measuring apparatus of abrasion of free rail of conveyor |
JPH11137907A (en) * | 1997-11-11 | 1999-05-25 | Moore Kk | Deaerator |
JP2008249508A (en) * | 2007-03-30 | 2008-10-16 | Nakanishi Metal Works Co Ltd | Wear inspection apparatus of conveyor rail |
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