JPH0438280Y2 - - Google Patents
Info
- Publication number
- JPH0438280Y2 JPH0438280Y2 JP3832887U JP3832887U JPH0438280Y2 JP H0438280 Y2 JPH0438280 Y2 JP H0438280Y2 JP 3832887 U JP3832887 U JP 3832887U JP 3832887 U JP3832887 U JP 3832887U JP H0438280 Y2 JPH0438280 Y2 JP H0438280Y2
- Authority
- JP
- Japan
- Prior art keywords
- liquefied gas
- sample
- gas
- cooling
- container
- 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
Links
- 238000001816 cooling Methods 0.000 claims description 17
- 239000007787 solid Substances 0.000 claims description 10
- 238000001514 detection method Methods 0.000 claims description 9
- 238000001073 sample cooling Methods 0.000 claims description 6
- 239000007789 gas Substances 0.000 description 75
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 238000001179 sorption measurement Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 6
- 238000003795 desorption Methods 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000009835 boiling Methods 0.000 description 3
- 239000003085 diluting agent Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
Landscapes
- Sampling And Sample Adjustment (AREA)
- Length Measuring Devices With Unspecified Measuring Means (AREA)
Description
【考案の詳細な説明】
産業上の利用分野
本考案は、粉体、粒体又は固体(以下固体と呼
ぶ)の表面積を測定する装置に関し、特にガスク
ロマトグラフにより固体の表面積を自動的に測定
する固体表面積測定装置に使用するのに適した試
料冷却用液化ガスの自動供給装置に関する。[Detailed description of the invention] Industrial application field This invention relates to an apparatus for measuring the surface area of powders, granules or solids (hereinafter referred to as solids), and in particular to an automatic supply device for liquefied gas for cooling samples that is suitable for use in a solid surface area measuring device that automatically measures the surface area of solids using a gas chromatograph.
従来の技術
従来、固体の表面積を測定する方法として、連
続流通系に於ける濃度測定法が実用化されている
が、この連続流通系に於ける濃度測定法
(Continuousflowガスクロマトグラフ法)は、吸
着ガスと不活性ガスの混合ガスを用い、その濃度
変化をガスクロマトグラフ的に追跡する方法であ
り、最終的には、BETの無限大吸着層に対する
等温式を用いて算出する。Conventional technology Conventionally, a concentration measurement method in a continuous flow system has been put into practical use as a method for measuring the surface area of a solid. This method uses a mixture of gas and inert gas and tracks its concentration changes using gas chromatography.The final calculation is performed using the isothermal equation for an infinite BET adsorption layer.
次に、連続流通系に於ける濃度表面積測定法
(ガスクロマトグラフ法)について簡単に説明す
る。 Next, a concentration surface area measurement method (gas chromatography method) in a continuous flow system will be briefly explained.
希釈ガス圧を調整する第1のバルブにより希釈
ガスを所定の流量に調整する。次に吸着ガス圧を
調整する第2のバルブにより吸着ガスを一定圧調
整してニードルバルブによりP/Poを調整する。
P/Poは0.1〜0.3の範囲で3値設定するのが通常
である。 A first valve that adjusts the dilution gas pressure adjusts the dilution gas to a predetermined flow rate. Next, the adsorbed gas is adjusted to a constant pressure using a second valve that adjusts the adsorbed gas pressure, and P/Po is adjusted using a needle valve.
P/Po is usually set to three values in the range of 0.1 to 0.3.
前記第1,第2のバルブ及びニードルバルブに
より調整された吸着ガスは、ストツプバルブを開
くことにより希釈剤と混合され、コールドトラツ
プ内に送り込まれる。ここで希釈剤及び吸着剤の
中の水分及び不純物質は除去されて熱伝導度検出
器の標準側を通過する。 The adsorbed gas adjusted by the first and second valves and the needle valve is mixed with the diluent by opening the stop valve, and is sent into the cold trap. Here, water and impurities in the diluent and adsorbent are removed and passed through the standard side of the thermal conductivity detector.
標準側を通過した混合ガスは試料管内の試料を
通過して熱伝導度検出器の検出側を通り外部へ排
出される。 The mixed gas that has passed through the standard side passes through the sample in the sample tube, passes through the detection side of the thermal conductivity detector, and is discharged to the outside.
今ここで、試料の温度が吸着ガスの沸点温度よ
りもはるかに高い場合、吸着ガスは試料に吸着さ
れることなく全量が検出側を通過する。従つて、
標準側を通過するガス組成と検出側を通過するガ
ス組成は全く同一であり検出器からの信号は変化
しない。 Now, if the temperature of the sample is much higher than the boiling point temperature of the adsorbed gas, the entire amount of the adsorbed gas passes through the detection side without being adsorbed by the sample. Therefore,
The gas composition passing through the standard side and the gas composition passing through the detection side are exactly the same, and the signal from the detector does not change.
次に、試料を吸着ガスの沸点まで冷却すると吸
着ガスは試料の表面に吸着され、標準側及び検出
側を通過するガス組成比が変化しその変化量に応
じた信号が発生する。しかしながら、やがて吸着
平衡に達すると検出器からの信号は冷却前の位置
で安定になる。 Next, when the sample is cooled to the boiling point of the adsorbed gas, the adsorbed gas is adsorbed on the surface of the sample, the gas composition ratio passing through the standard side and the detection side changes, and a signal is generated according to the amount of change. However, when adsorption equilibrium is eventually reached, the signal from the detector becomes stable at the position before cooling.
吸着平衡に達したのちに試料の冷却をやめる
と、試料に吸着された吸着ガスは脱着をはじめ混
合ガスに依つて検知側にはこばれる。このとき再
び標準側と検知側の濃度変化が起りそれに応じて
前とは逆の信号が発生する。 If cooling of the sample is stopped after reaching adsorption equilibrium, the adsorbed gas adsorbed to the sample will be blown to the detection side by desorption and the mixed gas. At this time, a concentration change occurs again on the standard side and the detection side, and a signal opposite to the previous one is generated accordingly.
この信号の大きさがある値の分圧比P/Poに
於ける吸着ガス量であり、この操作を各分圧比
P/Poに於て3点くり返し行い、吸着ガス量を
測定しB.E.Tの式により表面積を求めるのであ
る。吸着ガスの希釈剤としては普通Heを用い又
吸着ガスN2を用いている。従つて、冷却剤は液
体窒素(ligN2)を用いることになる。 The magnitude of this signal is the amount of adsorbed gas at a certain value of partial pressure ratio P/Po.This operation is repeated at three points at each partial pressure ratio P/Po, the amount of adsorbed gas is measured, and the amount of adsorbed gas is calculated using the BET formula. We are looking for the surface area. He is usually used as a diluent for the adsorbed gas, and N2 is used as the adsorbed gas. Therefore, liquid nitrogen (ligN2) will be used as a coolant.
考案が解決しようとする問題点
試料を吸着ガスの沸点まで冷却する場合には、
試料が収容された試料管を液体窒素等が収容され
た冷却用液化ガス容器に浸漬することによつて行
なわれるが、冷却用液化ガスは空気中に放置され
る結果、気化することにより時間の経過と共にそ
の量が減少する。従つて、その減少した分量を補
充する必要があるが、従来においては、その冷却
用液化ガス量を人手によつて監視し、必要に応じ
て必要量を補給していた。Problems that the invention aims to solve When cooling a sample to the boiling point of the adsorbed gas,
This is done by immersing the sample tube containing the sample into a cooling liquefied gas container containing liquid nitrogen, etc. However, as the cooling liquefied gas is left in the air, it evaporates and takes a long time. The amount decreases over time. Therefore, it is necessary to replenish the decreased amount, but conventionally, the amount of cooling liquefied gas has been manually monitored and the required amount has been replenished as necessary.
しかしながら、人手による人為的な方法による
ものであるから、わずらわしさが伴なうばかり
か、不測的ミスを惹起する欠点があつた。 However, since it is an artificial method, it is not only troublesome, but also has the drawback of causing unforeseen errors.
本考案は、従来の技術に内在する上記欠点を解
消する為になされたものであり、従つて本考案の
目的は、上記人為的操作をすべて自動化すること
によつて、不測的ミスの発生を未然に除去し、冷
却用液化ガス容器の必要に応じて必要量の液化ガ
スを自動的に補給することを可能とした新規な試
料冷却用液化ガスの自動供給装置を提供すること
にある。 The present invention was made in order to eliminate the above-mentioned drawbacks inherent in the conventional technology, and therefore, the purpose of the present invention is to automate all the above-mentioned human operations to prevent the occurrence of unexpected mistakes. It is an object of the present invention to provide a novel automatic supply device for a liquefied gas for cooling a sample, which is capable of removing the liquefied gas beforehand and automatically replenishing a required amount of liquefied gas to a cooling liquefied gas container as required.
問題点を解決する為の手段
上記目的を達成する為に、本考案に係る試料冷
却用液化ガスの自動供給装置は、固体の表面積を
測定する全自動表面積測定装置の回転ターンテー
ブル上に上下動自在に配設された試料冷却用液化
ガス容器に液化ガスを供給する装置であつて、前
記ターンテーブルに固定され該ターンテーブルと
共に回転する上部に第1の中空部を備えた回転軸
と、該回転軸の前記第1の中空部に連通しシール
結合された第2の中空部を有する固定軸と、該固
定軸に設けられ前記第2の中空部に連通する液化
ガス吸入導管と、前記回転軸に設けられ前記第1
の中空部に連通し且つその出口先端部が常に前記
試料冷却用液化ガス容器の上部に対向するように
配設された液化ガス供給導管と、前記液化ガス吸
入導管に連結された液化ガス供給源とを具備し、
更に、前記試料冷却用液化ガス容器内に液化ガス
の量を検出する検出器を設け、前記液化ガス吸入
導管と前記液化ガス供給源との間に前記検出器の
検出信号により作動する電磁弁を設けて構成され
る。Means for Solving the Problems In order to achieve the above object, an automatic sample cooling liquefied gas supply device according to the present invention is installed on a rotary turntable of a fully automatic surface area measuring device that measures the surface area of a solid. A device for supplying liquefied gas to freely disposed liquefied gas containers for sample cooling, the device comprising: a rotating shaft having a first hollow portion in an upper portion that is fixed to the turntable and rotates together with the turntable; a fixed shaft having a second hollow part communicating with and sealingly coupled to the first hollow part of the rotating shaft; a liquefied gas suction conduit provided on the fixed shaft and communicating with the second hollow part; provided on the shaft and said first
a liquefied gas supply conduit that communicates with the hollow part and is disposed such that its outlet end always faces the upper part of the liquefied gas container for cooling the sample; and a liquefied gas supply source connected to the liquefied gas suction conduit. and
Furthermore, a detector for detecting the amount of liquefied gas is provided in the sample cooling liquefied gas container, and a solenoid valve operated by a detection signal of the detector is provided between the liquefied gas suction conduit and the liquefied gas supply source. provided and configured.
実施例
次に本考案をその好ましい一実施例について図
面を参照しながら具体的に説明する。Embodiment Next, a preferred embodiment of the present invention will be specifically described with reference to the drawings.
第1図は本考案を含む固体表面積測定装置の一
部省略要部概略斜視図、第2図は本考案の一実施
例を示す主要部の断面図である。 FIG. 1 is a partially omitted schematic perspective view of the main parts of a solid surface area measuring apparatus including the present invention, and FIG. 2 is a sectional view of the main parts showing an embodiment of the present invention.
第1図〜第2図を参照するに、装置本体100
には、ターンテーブル10が駆動源30によつて
回転軸20Aを中心にして回転自在に設けられて
いる。ターンテーブル10上には、それぞれ等間
隔に試料焼出し用電気炉容器11、試料を冷却す
る液化ガス(例えば液体窒素)を収容する冷却用
液化ガス容器12及び脱着用水容器13が、それ
ぞれ、ピストン棒11b,12b及び13bを介
して上下動可能に装着されている。 Referring to FIGS. 1 and 2, a device main body 100
A turntable 10 is provided rotatably around a rotating shaft 20A by a drive source 30. On the turntable 10, an electric furnace container 11 for baking out the sample, a liquefied gas container 12 for cooling containing liquefied gas (for example, liquid nitrogen) for cooling the sample, and a water container 13 for desorption are arranged at equal intervals, respectively. It is mounted so as to be movable up and down via rods 11b, 12b and 13b.
回転軸20Aの上方部には固定軸20Bがシー
ル部34で連結されており、該固定軸20Bの周
囲には、例えば8個の試料に対応した8個の試料
管19が、導管21〜24を介して容器11,1
2,13の間隔と同一の間隔をもつてそれぞれ放
射状に固定されている。第2図には試料管19は
1個だけ示され、他は省略されている。 A fixed shaft 20B is connected to the upper part of the rotating shaft 20A by a sealing part 34, and around the fixed shaft 20B, eight sample tubes 19 corresponding to, for example, eight samples are connected to the conduits 21 to 24. via container 11,1
They are each fixed radially with the same spacing as the spacings 2 and 13. Only one sample tube 19 is shown in FIG. 2, and the others are omitted.
装置本体100の上部には、焼出し用ガス流路
切換コツク15,17又は吸、脱着用ガス流路切
換コツク16,18がそれぞれ同一の駆動モータ
37により2個の連結ギヤ35,36を介して同
時に動作するように配設されている。 On the upper part of the apparatus main body 100, gas passage switching sockets 15, 17 for baking out or gas passage switching sockets 16, 18 for suction and desorption are connected by the same drive motor 37 via two connecting gears 35, 36, respectively. are arranged to operate simultaneously.
上記構成において、ターンテーブル10が矢印
の方向に回転すると共に、必要に応じて容器11
〜13が上下動して試料管19を収容又は開放す
ることによつて、複数の試料を同時に処理し、試
料の焼出し、ガスの吸着、脱着が自動化されて連
続的に実行される。 In the above configuration, the turntable 10 rotates in the direction of the arrow, and the container 11 is rotated as needed.
- 13 move up and down to accommodate or open the sample tube 19, thereby processing a plurality of samples simultaneously, and baking out the samples, gas adsorption, and desorption are automated and continuously executed.
冷却用液化ガス容器(吸着用)12には、例え
ば液体窒素の如き液化ガスが充填されており、そ
の液化ガスの量を検出する検出器31が配設され
ている。液化ガスとして液体窒素が使用された場
合には検出器31として約−198℃の温度センサ
が使用される。更に第2図に見られる如く、中空
部20B′を有する円筒体により形成された固定
軸20Bには液化ガス吸入導管32が形成されて
いる。更に、0リングシール40により固定軸2
0Bに回転自在に連結された回転軸20Aの上部
には中空部20B′と連通する中空部20A′が形
成されると共に、その中空部20A′と連通する
液化ガス供給導管33が突出して形成されてい
る。導管33の出口33aは液化ガス容器12の
入口に対向させられている。また、27は冷却用
液化ガステユワピン(液化ガス供給源)を示し、
このテユワビン27は供給パイプ28及び電磁弁
41を介して前記液化ガス吸入導管32に結合さ
れている。 The cooling liquefied gas container (for adsorption) 12 is filled with liquefied gas such as liquid nitrogen, and is provided with a detector 31 that detects the amount of the liquefied gas. When liquid nitrogen is used as the liquefied gas, a temperature sensor of about -198° C. is used as the detector 31. Furthermore, as seen in FIG. 2, a liquefied gas suction conduit 32 is formed in the fixed shaft 20B formed of a cylindrical body having a hollow portion 20B'. Furthermore, the fixed shaft 2 is secured by the O-ring seal 40.
A hollow part 20A' that communicates with the hollow part 20B' is formed in the upper part of the rotating shaft 20A that is rotatably connected to the rotary shaft 20A, and a liquefied gas supply conduit 33 that communicates with the hollow part 20A' is formed to protrude. ing. The outlet 33a of the conduit 33 is opposed to the inlet of the liquefied gas container 12. In addition, 27 indicates a cooling liquefied gas steering pin (liquefied gas supply source),
The wafer bin 27 is connected to the liquefied gas suction conduit 32 via a supply pipe 28 and a solenoid valve 41.
次に動作について説明する。ターンテーブル1
0、液化ガス容器12、液化ガス供給導管33は
回転軸20Aに固定されているので、回転軸20
Aと共に回転し、これらは常に第2図に示された
状態を維持している。今、容器12中の冷却用液
化ガスが減少して検出器31が液化ガスの面から
離れる際には温度が上昇して検出器31が動作
し、その検出信号により電磁弁41が付勢されて
電磁弁41が開かれる。その結果、冷却用液化ガ
スデユワビン27から、供給パイプ28、電磁弁
41、導管32、中空部20B′、中空部20
A′及び導管33によつて形成される流路を介し
て、液化ガスが容器12に供給される。容器12
内の液化ガスが予め定められた規定値に達する
と、検出器31の動作が停止し、電磁弁41が減
勢されて前記流路が遮断される結果、容器12へ
の液体ガスの供給は停止される。以上の動作が自
動的に繰り返されて、容器12には常に所望の液
化ガスが充填されることになる。 Next, the operation will be explained. Turntable 1
0, since the liquefied gas container 12 and the liquefied gas supply conduit 33 are fixed to the rotating shaft 20A, the rotating shaft 20
A rotates with A, and they always maintain the state shown in FIG. Now, when the cooling liquefied gas in the container 12 decreases and the detector 31 moves away from the surface of the liquefied gas, the temperature rises and the detector 31 operates, and the solenoid valve 41 is energized by the detection signal. The solenoid valve 41 is opened. As a result, the supply pipe 28, the solenoid valve 41, the conduit 32, the hollow part 20B', the hollow part 20
Liquefied gas is supplied to the container 12 via the channel formed by A' and the conduit 33. container 12
When the liquefied gas in the container reaches a predetermined value, the detector 31 stops operating, the solenoid valve 41 is deenergized, and the flow path is cut off, so that the supply of liquid gas to the container 12 is stopped. will be stopped. The above operations are automatically repeated, and the container 12 is always filled with the desired liquefied gas.
考案の効果
本考案は以上の如く構成され、作用するもので
あり、本考案によれば、液化ガス容器に常時必要
量の液化ガスが自動的に充填されているので、連
続的自動処理動作にもかかわらず、吸着ガスの試
料に対する吸着作用が良好にしかも的確に行わ
れ、迅速にして確実な固体表面積の測定を実現で
きる効果が得られる。Effects of the invention The present invention is constructed and operates as described above. According to the invention, the liquefied gas container is automatically filled with the required amount of liquefied gas at all times, so that continuous automatic processing operation is possible. Nevertheless, the adsorption effect of the adsorbed gas on the sample is performed well and accurately, and the effect of realizing rapid and reliable measurement of the solid surface area is obtained.
第1図は本考案が適用される固体表面積測定装
置の概略斜視図、第2図は本考案の一実施例を示
す概略断面図である。
10……ターンテーブル、11……焼出し用電
気炉容器、12……冷却用液化ガス容器(吸着
用)、13……脱着用水容器、20A……回転軸、
20B……固定軸、27……液化ガスデユワビン
(液化ガス供給源)、28……供給パイプ、30…
…ターンテーブル駆動源、31……液化ガス量検
出器、32……液化ガス吸入導管、33……液化
ガス供給導管、34……固定軸、回転軸シール
部、40……0リングシール、41……電磁弁。
FIG. 1 is a schematic perspective view of a solid surface area measuring device to which the present invention is applied, and FIG. 2 is a schematic sectional view showing an embodiment of the present invention. 10... Turntable, 11... Electric furnace container for baking out, 12... Liquefied gas container for cooling (for adsorption), 13... Water container for desorption, 20A... Rotating shaft,
20B...Fixed shaft, 27...Liquefied gas duplex (liquefied gas supply source), 28...Supply pipe, 30...
... Turntable drive source, 31 ... Liquefied gas amount detector, 32 ... Liquefied gas suction conduit, 33 ... Liquefied gas supply pipe, 34 ... Fixed shaft, rotating shaft seal section, 40 ... O-ring seal, 41 ……solenoid valve.
Claims (1)
置の回転ターンテーブル上に上下動自在に配設
された試料冷却用液化ガス容器に液化ガスを供
給する装置であつて、前記ターンテーブルに固
定され該ターンテーブルと共に回転する上部に
第1の中空部を備えた回転軸と、該回転軸の前
記第1の中空部に連通しシール結合された第2
の中空部を有する固定軸と、該固定軸に設けら
れ前記第2の中空部に連通する液化ガス吸入導
管と、前記回転軸に設けられ前記第1の中空部
に連通し且つその出口先端部が常に前記試料冷
却用液化ガス容器の上部に対向するように配設
された液化ガス供給導管と、前記液化ガス吸入
導管に連結された液化ガス供給源とを具備する
ことを特徴とした試料冷却用液化ガスの自動供
給装置。 (2) 前記試料冷却用液化ガス容器内に液化ガスの
量を検出する検出器を設け、前記液化ガス吸入
導管と前記液化ガス供給源との間に前記検出器
の検出信号により作動する電磁弁を設けたこと
を更に特徴とする実用新案登録請求の範囲第(1)
項に記載の試料冷却用液化ガスの自動供給装
置。[Scope of Claim for Utility Model Registration] (1) A device for supplying liquefied gas to a liquefied gas container for cooling a sample that is vertically movable on a rotary turntable of a fully automatic surface area measuring device that measures the surface area of a solid. a rotating shaft that is fixed to the turntable and rotates together with the turntable and has a first hollow section in its upper part;
a fixed shaft having a hollow portion; a liquefied gas suction conduit provided on the fixed shaft and communicating with the second hollow portion; and an outlet tip portion of the fixed shaft provided on the rotating shaft and communicating with the first hollow portion. a liquefied gas supply conduit arranged so as to always face the upper part of the liquefied gas container for sample cooling, and a liquefied gas supply source connected to the liquefied gas suction conduit. Automatic supply device for liquefied gas. (2) A detector for detecting the amount of liquefied gas is provided in the sample cooling liquefied gas container, and a solenoid valve is provided between the liquefied gas suction conduit and the liquefied gas supply source and is operated by a detection signal from the detector. Scope of Claim for Utility Model Registration No. (1), which is further characterized in that
An automatic supply device for liquefied gas for sample cooling as described in 2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3832887U JPH0438280Y2 (en) | 1987-03-16 | 1987-03-16 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3832887U JPH0438280Y2 (en) | 1987-03-16 | 1987-03-16 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63145153U JPS63145153U (en) | 1988-09-26 |
| JPH0438280Y2 true JPH0438280Y2 (en) | 1992-09-08 |
Family
ID=30850468
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3832887U Expired JPH0438280Y2 (en) | 1987-03-16 | 1987-03-16 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0438280Y2 (en) |
-
1987
- 1987-03-16 JP JP3832887U patent/JPH0438280Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63145153U (en) | 1988-09-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5792423A (en) | Headspace autosampler apparatus and method | |
| US2833151A (en) | Device for delivering measured quantities of gases or vapours | |
| US5932482A (en) | Headspace vial apparatus and method | |
| US3498110A (en) | Method and apparatus for measuring the gas and vapor permeability of films | |
| US5107696A (en) | Device for measuring gas permeation | |
| US4063446A (en) | Method of and apparatus for automatically detecting traces of organic solvent vapors in air | |
| US4359891A (en) | Repetitive chromatographic apparatus | |
| US5159829A (en) | Device for measuring gas permeation | |
| US4399688A (en) | Air pollution detection | |
| US3249403A (en) | Liquid sample reactor and evolved gas detector | |
| JPH0438280Y2 (en) | ||
| US5789258A (en) | Method for generating vapor streams | |
| US5996397A (en) | Reactive gas sampling/analyzing hygrometry system | |
| JP3138009B2 (en) | Method and apparatus for evaluating impurity adsorption amount | |
| US10591936B2 (en) | Devices, systems and methods for purging and loading sorbent tubes | |
| US4045998A (en) | Temperature control system | |
| JPS5828650A (en) | Specific surface area measuring device | |
| US5109714A (en) | Method and means for dynamic measurement of rates of adsorption from solutions | |
| US5734097A (en) | Analyzer and method for measuring water in liquids | |
| JPH04329337A (en) | Measuring method for gas permeability of film | |
| JP2005069870A (en) | Infrared gas analyzer | |
| JP3097177B2 (en) | Surface area measuring device | |
| SU1244096A1 (en) | Device for studying kinetics of film material steam permeability | |
| JPH11174035A (en) | Gas chromatograph | |
| US2538498A (en) | Method and apparatus for determining toxicity |