JPS5910247B2 - Solvent mixing liquid delivery device - Google Patents
Solvent mixing liquid delivery deviceInfo
- Publication number
- JPS5910247B2 JPS5910247B2 JP56133137A JP13313781A JPS5910247B2 JP S5910247 B2 JPS5910247 B2 JP S5910247B2 JP 56133137 A JP56133137 A JP 56133137A JP 13313781 A JP13313781 A JP 13313781A JP S5910247 B2 JPS5910247 B2 JP S5910247B2
- Authority
- JP
- Japan
- Prior art keywords
- solvent
- helium gas
- section
- flow path
- mixing
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Description
【発明の詳細な説明】
この発明は溶媒混合送液装置に関し、特に溶媒溜めと溶
媒混合部との間の溶媒流路に、合成樹脂膜を介して、溶
媒中の空気とヘリウムガスが置換できるように、ヘリウ
ムガス流路を接触させることによつて溶媒混合時の気泡
発生を防止し、それによつてポンプによる定量送液を可
能にするものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a solvent mixing and liquid feeding device, and in particular, to a solvent flow path between a solvent reservoir and a solvent mixing section, air and helium gas in the solvent can be replaced through a synthetic resin membrane. By bringing the helium gas channels into contact with each other, the generation of bubbles during solvent mixing is prevented, thereby making it possible to deliver a fixed amount of liquid using a pump.
溶媒は通常空気に触れており、空気の溶融はさけられな
い。Solvents are usually exposed to air, and melting of the air is unavoidable.
一方、高速液体クロマトグラフなどでは溶媒を混合して
一定量ポンプで送液する必要がある。例えば水とメタノ
ール(又はアセトニトリル)の混合送液を行なう場合、
両液が混合を始めると混合液に対する空気の溶解量が、
各々の液の溶解量の和より小さいため(第1図参照)、
空気が過飽和となつて気泡となる。従つてこのような気
泡を含んだ混合液をポンプに供給しても到底定量送液は
望めない。これらの問題を解決する手段としては、溶媒
混合部とポンプの間に気液分離部を設けることが知られ
ているが、分離部における容積が組成変化の遅れをもた
らし、更に脱ガス操作にともなう組成の変動をまねくな
ど性能的に多くの問題が生じる。On the other hand, in high performance liquid chromatographs and the like, it is necessary to mix solvents and pump them in a fixed amount. For example, when feeding a mixture of water and methanol (or acetonitrile),
When both liquids start mixing, the amount of air dissolved in the mixed liquid is
Because it is smaller than the sum of the dissolved amounts of each solution (see Figure 1),
Air becomes supersaturated and forms bubbles. Therefore, even if a mixed liquid containing such bubbles is supplied to a pump, it is impossible to expect a constant amount of liquid delivery. As a means to solve these problems, it is known to provide a gas-liquid separation section between the solvent mixing section and the pump, but the volume in the separation section causes a delay in composition change, and furthermore, the degassing operation causes problems. Many problems arise in terms of performance, such as compositional fluctuations.
この発明者らは、これらの事情に鑑み鋭意研究を重ね、
合成樹脂薄層を各種の分子が透過する現象に着目し、そ
の薄層を溶媒から発生した気泡の透過に利用できること
を見出し、この発明を完成するに至つたものである。す
なわち、この発明の具体的な構成は、複数の溶媒溜めと
、これらの溶媒の混合部と、混合溶媒の送液ポンプとを
備え、更に溶媒溜めと混合部と・ の間の溶媒流路に、
溶媒中の空気とヘリウムガスとの置換部を介設してなる
溶媒混合送液装置である。In view of these circumstances, the inventors conducted extensive research, and
Focusing on the phenomenon that various molecules permeate through a thin layer of synthetic resin, they discovered that the thin layer could be used to permeate bubbles generated from a solvent, leading to the completion of this invention. That is, the specific configuration of the present invention includes a plurality of solvent reservoirs, a mixing section for these solvents, and a liquid delivery pump for the mixed solvent, and a solvent flow path between the solvent reservoirs and the mixing section. ,
This is a solvent mixing/liquid feeding device that includes a replacement section for replacing air in the solvent with helium gas.
つまり、この発明は、溶媒溜めと混合部との間の溶媒流
路に、溶媒が流れる合成樹脂製粒路と、フその外側を覆
うヘリウムガス流路とからなる溶媒中の空気とヘリウム
ガスとの置換部を介設することによつて、溶媒中に溶解
している空気を、流路を通して空気分圧の小さいヘリウ
ムガス側へ透過させ、それによつて溶解空気の量を減ら
し混合部ク での気泡発生を防止し、定量送液を可能に
するものである。In other words, in this invention, the solvent flow path between the solvent reservoir and the mixing section has a synthetic resin granule path through which the solvent flows, and a helium gas flow path that covers the outside of the holder. By providing a displacement part in the mixing part, the air dissolved in the solvent is allowed to permeate through the flow path to the helium gas side where the air partial pressure is small, thereby reducing the amount of dissolved air. This prevents the generation of bubbles and enables fixed-quantity liquid delivery.
もちろんヘリウムガスは、逆に膜を通して溶媒側へ移行
するが、各種溶媒に対する溶解度が最も小さいので、混
合時の気泡発生のおそれはほとんどない。この発明に}
いて使用可能な合成樹脂製流路としては、4弗化エチレ
ン樹脂、ポリエチレン樹脂、などの流路が好ましく、最
も好ましいものとしてほとんどの溶媒に対して安定な4
弗化エチレン樹脂(テフロン:登録商標)パイプ製が挙
げられる。Of course, helium gas moves through the membrane to the solvent side, but since it has the lowest solubility in various solvents, there is almost no risk of bubbles occurring during mixing. To this invention}
As the synthetic resin flow path that can be used in the process, it is preferable to use a flow path made of tetrafluoroethylene resin, polyethylene resin, etc.
Examples include those made of fluorinated ethylene resin (Teflon: registered trademark) pipes.
パイプの肉厚としては、4弗化エチレン樹脂の場合、0
.1〜Im程度が望ましい。これらの合成樹脂製パイプ
の内経は0.5〜2mmφが好ましい。以下図に示す実
施例に基づいてこの発明を詳述する。なお、これによつ
てこの発明が限定を受けるものではない。第2図におい
て、溶媒混合送液装置1は二つの溶媒の吸引流路2,3
と、溶媒混合部4と、混合溶媒液ポンプ5とから主とし
て構成されている。The wall thickness of the pipe is 0 in the case of tetrafluoroethylene resin.
.. A value of about 1 to Im is desirable. The inner diameter of these synthetic resin pipes is preferably 0.5 to 2 mmφ. The present invention will be described in detail below based on embodiments shown in the figures. Note that this invention is not limited by this. In FIG. 2, a solvent mixing liquid feeding device 1 has two solvent suction channels 2 and 3.
, a solvent mixing section 4 , and a mixed solvent liquid pump 5 .
吸引流路2は、メタノールの溶媒溜め6からへリウムガ
ス接触部7及び時間比例弁8を経て溶媒混合部4に至る
。ヘリウムガス接触部7は、溶媒中の空気とヘリウムガ
スとの置換部と称すこともでき、溶媒の流路20を4弗
化エチレン樹脂製の細管(内径Imφ)をコイル状とし
、その周囲に同軸に円筒状のステンレス製ヘリウムガス
流路9を形成している。10はヘリウムガス入口、11
は出口である。The suction channel 2 extends from a methanol solvent reservoir 6 to a solvent mixing section 4 via a helium gas contact section 7 and a time proportional valve 8. The helium gas contact section 7 can also be referred to as a section for replacing air in the solvent with helium gas. A cylindrical stainless steel helium gas channel 9 is coaxially formed. 10 is helium gas inlet, 11
is the exit.
なお、12はフイルタである。一方、吸引流路3の構成
は、溶媒が水である以外同一であるので説明を省略する
。溶媒混合送液装置1は、送液ポンプ5及び時間比例弁
8,13の開作動によりメタノールと水が各溶媒溜め6
,14から吸引されて混合し、高速液体クロマトグラフ
へ移送される。Note that 12 is a filter. On the other hand, the configuration of the suction flow path 3 is the same except that the solvent is water, so the explanation will be omitted. In the solvent mixing liquid feeding device 1, methanol and water are supplied to each solvent reservoir 6 by opening the liquid feeding pump 5 and the time proportional valves 8 and 13.
, 14, mixed, and transferred to a high performance liquid chromatograph.
この際、例えばメタノールがヘリウムガス接触部7を通
過すると、その細管の4弗化エチレン樹脂薄層の外に空
気分圧がほぼ零のヘリウムガス空間が存在しているので
、空気分圧差が大きく、メタノール中の溶解空気が薄層
を透過してヘリウムガス流路側に脱出しヘリウムガスと
共に出口11から適宜系外へ運ばれる。もちろん、ヘリ
ウムガスは、逆に薄層を透過してメタノール中に溶解し
置換されるが、溶解度がきわめて低い。一方の水の場合
も同様にしてヘリウムガス側へ溶解空気が脱出する。か
くして溶解空気濃度が低下したメタノールと水は混合し
てもほとんど気泡を発生することがなく、従つてきわめ
て正確に定量送液が可能になる。従来の脱気法である溶
媒中へのヘリウムガスのバプリングによるものは、ヘリ
ウムガスと溶媒が直接接触しているので、ヘリウムガス
の流れにのつて、溶媒の分子が相当量失われることがあ
り、塩類を溶解した水溶液などの場合は特に濃度変化が
問題になる。しかし以上の装置では、溶媒とヘリウムガ
スの間に合成樹脂薄層が介在するので溶媒濃度(組成)
変化を少なくできる。な}、溶媒中の空汽とヘリウムガ
スとの置換部は、密閉容器を4弗化エチレン樹脂製の薄
膜21aで区画し、一方を溶媒の流路20aとして、他
方をヘリウムガスの流路9aとしてそれぞれ用いること
もできる(第3図参照)。At this time, for example, when methanol passes through the helium gas contact part 7, there is a helium gas space with almost zero air partial pressure outside the thin layer of tetrafluoroethylene resin in the thin tube, so the air partial pressure difference is large. The air dissolved in methanol passes through the thin layer and escapes to the helium gas flow path side, and is appropriately carried out of the system from the outlet 11 along with the helium gas. Of course, helium gas permeates through the thin layer and dissolves in methanol, replacing it, but its solubility is extremely low. In the case of water, dissolved air escapes to the helium gas side in the same way. Methanol and water, which have a reduced concentration of dissolved air in this way, hardly generate any bubbles when mixed, making it possible to feed the liquid in a fixed amount with great accuracy. Traditional degassing methods that involve bubbling helium gas into the solvent involve direct contact between the helium gas and the solvent, which can result in a significant amount of solvent molecules being lost in the flow of helium gas. In the case of aqueous solutions containing dissolved salts, concentration changes are particularly problematic. However, in the above device, a thin layer of synthetic resin is interposed between the solvent and helium gas, so the solvent concentration (composition)
Changes can be reduced. In order to replace the air steam in the solvent with helium gas, the airtight container is divided by a thin film 21a made of tetrafluoroethylene resin, and one side is used as the solvent flow path 20a and the other side is used as the helium gas flow path 9a. (See Figure 3).
第1図は水とメタノールに対する空気の溶解量を示すグ
ラフ、第2図はこの発明の溶媒混合送液装置の一実施例
を示す機能説明図、第3図は他の実施例を示す要部機能
説明図である。
1・・・・・・溶媒混合送液装置、2,3・・・・・・
吸引流路、4・・・・・・溶媒混合部、5・・・・・・
送液ポンプ、6,14・・・・・・溶媒溜め、7,15
・・・・・・ヘリウムガス接触部、9,18・・・・・
・ヘリウムガス流路。Fig. 1 is a graph showing the amount of air dissolved in water and methanol, Fig. 2 is a functional explanatory diagram showing one embodiment of the solvent mixing liquid feeding device of the present invention, and Fig. 3 is a main part showing another embodiment. It is a functional explanatory diagram. 1... Solvent mixing liquid feeding device, 2, 3...
Suction channel, 4... Solvent mixing section, 5...
Liquid feed pump, 6, 14...Solvent reservoir, 7, 15
・・・・・・Helium gas contact part, 9, 18・・・・・・
・Helium gas flow path.
Claims (1)
溶媒の送液ポンプとを備え、更に溶媒溜めと混合部との
間の溶媒流路に、溶媒中の空気とヘリウムガスとの置換
部を介設してなる溶媒混合送液装置。 2 置換部の溶媒流路とヘリウムガス流路とが合成樹脂
製薄膜を介して相接している特許請求の範囲第1項に記
載の装置。 3 置換部が、合成樹脂製の溶媒流路とその外側に覆う
ように形成されたヘリウムガス流路とから構成される特
許請求の範囲第1項又は第2項に記載の装置。 4 合成樹脂として4弗化エチレン樹脂を用いる特許請
求の範囲第1〜3項のいずれかに記載の装置。[Claims] 1. A system comprising a plurality of solvent reservoirs, a mixing section for these solvents, and a liquid delivery pump for the mixed solvent, and further includes a solvent passageway between the solvent reservoirs and the mixing section for supplying air in the solvent. A solvent mixing liquid feeding device that includes a replacement section for replacing helium gas with helium gas. 2. The apparatus according to claim 1, wherein the solvent flow path and the helium gas flow path of the substitution section are in contact with each other via a synthetic resin thin film. 3. The apparatus according to claim 1 or 2, wherein the substitution section is comprised of a synthetic resin solvent channel and a helium gas channel formed to cover the outside of the solvent channel. 4. The device according to any one of claims 1 to 3, using tetrafluoroethylene resin as the synthetic resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56133137A JPS5910247B2 (en) | 1981-08-24 | 1981-08-24 | Solvent mixing liquid delivery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56133137A JPS5910247B2 (en) | 1981-08-24 | 1981-08-24 | Solvent mixing liquid delivery device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5834031A JPS5834031A (en) | 1983-02-28 |
| JPS5910247B2 true JPS5910247B2 (en) | 1984-03-07 |
Family
ID=15097623
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56133137A Expired JPS5910247B2 (en) | 1981-08-24 | 1981-08-24 | Solvent mixing liquid delivery device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5910247B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03154601A (en) * | 1989-11-10 | 1991-07-02 | Ebara Infilco Co Ltd | Removal of dissolving oxygen in water |
-
1981
- 1981-08-24 JP JP56133137A patent/JPS5910247B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5834031A (en) | 1983-02-28 |
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