JPH0682433A - Floating sampler - Google Patents
Floating samplerInfo
- Publication number
- JPH0682433A JPH0682433A JP23188692A JP23188692A JPH0682433A JP H0682433 A JPH0682433 A JP H0682433A JP 23188692 A JP23188692 A JP 23188692A JP 23188692 A JP23188692 A JP 23188692A JP H0682433 A JPH0682433 A JP H0682433A
- Authority
- JP
- Japan
- Prior art keywords
- container
- liquid
- tube
- gas
- sampler
- 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
Landscapes
- Sampling And Sample Adjustment (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明はプロセスガスクロマトグ
ラフ(以下PGCという)のサンプラに関し,コストの
低減と保守の容易化を図ったサンプラに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sampler for a process gas chromatograph (hereinafter referred to as PGC), and more particularly to a sampler with reduced cost and easy maintenance.
【0002】[0002]
【従来の技術】図2はサンプラを含むPGCの従来例を
示す概略構成図である。図において1は例えばビール工
場の醗酵槽,2は醗酵液である。3は上部バルブであ
り,この上部バルブ3を介して取り入れられたサンプル
液はサンプルコンディショナ4に送られて減圧,減
(加)温,徐塵,流量の調節等が行われる。そしてこの
コンディショナ4から送出されたサンプル液は分析計5
に送られてサンプルに含まれるガスの分析が行われる。
なお,使用後のサンプル液はポンプ6,下部バルブ7を
介して醗酵槽に戻される。2. Description of the Related Art FIG. 2 is a schematic configuration diagram showing a conventional PGC including a sampler. In the figure, 1 is a fermentation tank of a beer factory, and 2 is a fermentation liquid. Reference numeral 3 is an upper valve, and the sample liquid taken in through the upper valve 3 is sent to a sample conditioner 4 to be subjected to depressurization, reduction (heating) temperature, dust removal, flow rate adjustment, and the like. The sample liquid sent from the conditioner 4 is analyzed by the analyzer 5.
The gas contained in the sample is sent to and analyzed.
The used sample solution is returned to the fermentor via the pump 6 and the lower valve 7.
【0003】[0003]
【発明が解決しようとする課題】このような装置におい
てはサンプル液をバルブやパイプを介して移送している
ので液の粘度が高い場合はラインの閉塞や,サンプルが
減圧,減(加)温される為に組成が変化する等の問題が
あり,また,醗酵槽にサンプル液を戻す場合にポンプを
使用するとコスト増となり保守作業も発生する。本発明
は上記従来技術の問題点を解決するためになされたもの
で,バルブやパイプが閉塞したり組成変化の恐れがな
く,サンプル液を醗酵槽に戻す必要のないサンプラを実
現することにある。In such an apparatus, since the sample liquid is transferred through a valve or a pipe, when the viscosity of the liquid is high, the line is blocked or the sample is depressurized or heated (heated). Therefore, there is a problem that the composition changes, and when a pump is used to return the sample liquid to the fermenter, the cost increases and maintenance work is required. The present invention has been made to solve the above-mentioned problems of the prior art, and is to realize a sampler that does not have a risk of blockage of valves and pipes or composition change and does not need to return a sample solution to a fermenter. .
【0004】[0004]
【課題を解決するための手段】上記課題を解決する為に
本発明は,気体は浸透し,液体は浸透しない部材で形成
されたガス採集容器と,該容器中に配置された不活性部
材からなる重りと,前記容器中に一端が挿入され外周が
気密に固定された少なくとも2本のチューブからなり,
前記容器をプロセス液体に浸漬するとともに前記チュー
ブの一方の他端から前記容器内にキャリアガスを導入
し,前記チューブの他方の他端を分析計側に接続したこ
とを特徴とするものである。In order to solve the above problems, the present invention comprises a gas collection container formed of a member that allows gas to permeate therethrough and does not allow liquid to permeate, and an inert member disposed in the container. A weight and at least two tubes, one end of which is inserted into the container and the outer periphery of which is hermetically fixed,
The container is immersed in a process liquid, a carrier gas is introduced into the container from one end of the tube, and the other end of the tube is connected to an analyzer side.
【0005】[0005]
【作用】ガス採集容器を醗酵槽に入れると,この容器は
液体の密度とキャリアガスが満たされる容積と不活性材
からなる重りとのバランスにより一部(若しくは全部)
が液に浸漬した状態となる。ガス収集容器は気体は浸透
し,液体は浸透しない部材で出来ているので液体に含ま
れるガスが浸透する。このガスは他方のチューブを介し
て取り出されて分析計に向かう。[Operation] When a gas collection container is put in the fermenter, this container is partially (or entirely) depending on the balance of the density of the liquid, the volume filled with the carrier gas, and the weight made of the inert material.
Is immersed in the liquid. Since the gas collection container is made of a member that allows gas to permeate and liquid does not, the gas contained in the liquid permeates. This gas is withdrawn via the other tube towards the analyzer.
【0006】[0006]
【実施例】以下図面に従い本発明のサンプラを説明す
る。図1は本発明の一実施例を示す構成図である。図に
おいて1は例えばビール工場の醗酵槽,2は醗酵液であ
る。10は分子量の小さいガス或いは揮発性成分は浸透
し,分子量の大きい液体は浸透しない部材(高分子膜)
からなるガス採集容器であり,この容器10には液体と
の接触面積を任意の位置に保持するための重りである不
活性金属(例えばステンレス鋼)11が収納されてい
る。12はシール部材であり容器10にはこのシール部
材により外周がシールされた第1,第2チューブ13,
14の一端が挿入されている。DESCRIPTION OF THE PREFERRED EMBODIMENTS A sampler of the present invention will be described below with reference to the drawings. FIG. 1 is a block diagram showing an embodiment of the present invention. In the figure, 1 is a fermentation tank of a beer factory, and 2 is a fermentation liquid. No. 10 is a member (polymer film) that allows gas or volatile components with a low molecular weight to permeate, but does not allow liquids with a high molecular weight to permeate.
The container 10 contains an inert metal (for example, stainless steel) 11 which is a weight for holding the contact area with the liquid at an arbitrary position. Reference numeral 12 denotes a seal member, and the container 10 has first and second tubes 13 whose outer periphery is sealed by the seal member.
One end of 14 is inserted.
【0007】そして,第1チューブの他端側はキャリア
ガス送出部17に接続されている。このキャリアガス送
出部17は圧力調節弁18,圧力計19を備えており,
圧力調節弁18の一端にはキャリアガスとして機能する
不活性ガス(例えばN2,He,Arガス等)のボンベ
(図示せず)が接続されている。一方第2チューブ14
の他端は流量調節部20を構成するニードル弁21に接
続されており,流量計22を介して分析計に送出され
る。25は醗酵槽内の圧力を含む所定の深さの液圧を測
定するための圧力計である。The other end of the first tube is connected to the carrier gas delivery section 17. The carrier gas delivery unit 17 is equipped with a pressure control valve 18 and a pressure gauge 19,
One end of the pressure regulating valve 18 (not shown) cylinder of inert gas serving as a carrier gas (e.g. N 2, H e, A r gas, etc.) are connected. On the other hand, the second tube 14
The other end of is connected to a needle valve 21 that constitutes the flow rate controller 20, and is sent to the analyzer via a flow meter 22. Reference numeral 25 is a pressure gauge for measuring the liquid pressure at a predetermined depth including the pressure inside the fermentor.
【0008】上記の構成において,ガス採集容器10が
布状の高分子膜であるとし,これを醗酵液に浸漬すると
この容器は重り11により液中に沈む。しかし第1チュ
ーブ13の他端からキャリアガスを容器10に送出する
と,この容器は重り11とバランスしたところで安定す
る。なお,キャリアガスの圧力は圧力計25の圧力をみ
ながらこれより高い圧力で送出する必要があるが,容器
をどの位置で安定させるかはゴアテックスを浸透して来
るガス量によって決定する。In the above construction, the gas collection container 10 is a cloth-like polymer film, and when it is immersed in the fermentation liquid, the container is submerged in the liquid by the weight 11. However, when the carrier gas is delivered from the other end of the first tube 13 to the container 10, the container becomes stable when it is balanced with the weight 11. The pressure of the carrier gas needs to be sent at a higher pressure than the pressure of the pressure gauge 25, but the position of stabilizing the container is determined by the amount of gas that permeates the GORE-TEX.
【0009】容器10に浸透したガスはキャリアガスと
共に第2チューブ14の一端から送出されニードル弁2
1,流量計22を通って分析計に送出される。なお,本
実施例においてはプロセスの一例として醗酵槽をあげて
説明したが,本実施例に限ることなく種々のプロセスに
応用することが可能であり,ガス採集容器10は測定プ
ロセスの粘性やスラリー状であるか否かや温度等に応じ
て適宜適切なものを選択するものとする。また,容器1
0内に挿入するチューブも2本に限ることなく必要に応
じて増加することも可能である。The gas that has permeated the container 10 is sent out from one end of the second tube 14 together with the carrier gas, and the needle valve 2
1, through the flowmeter 22 to the analyzer. In the present embodiment, a fermenter was described as an example of the process, but the present invention is not limited to this embodiment and can be applied to various processes. Appropriate ones should be selected according to whether or not they are in a shape, temperature, and the like. Also, container 1
The number of tubes inserted into 0 is not limited to two, and it is possible to increase the number as necessary.
【0010】[0010]
【発明の効果】以上実施例とともに具体的に説明した様
に本発明によれば,サンプルの採取がプロセス内(イン
ライン)で行われるため,従来のようなサンプルコンデ
ィショナを必要としない。従ってコストが安く,保守も
軽減される。また,重質成分/タール/ダスト(粒子)
等を含むプロセス液体にも適用できる。更にガス採集容
器の容積は必要に応じて小型化が可能なのでプロセスか
らのサンプルの実質の採取量を微量にすることも可能で
ある。従って小規模(小容量)のプロセスでもサンプル
取出しによる外乱も起こり難くなり,取り出したサンプ
ルの廃棄処理も容易である。As described above in detail with reference to the embodiments, according to the present invention, since a sample is taken in the process (in-line), a conventional sample conditioner is not required. Therefore, the cost is low and maintenance is reduced. Also, heavy components / tar / dust (particles)
It can also be applied to process liquids such as. Further, since the volume of the gas collection container can be reduced as necessary, it is also possible to make the actual amount of sample collected from the process small. Therefore, even in a small-scale (small-volume) process, disturbance due to sample withdrawal is less likely to occur, and the sample withdrawn can be easily discarded.
【図1】本発明のフローティング・サンプラの一実施例
を示す構成図である。FIG. 1 is a configuration diagram showing an embodiment of a floating sampler of the present invention.
【図2】従来のフローティング・サンプラの一例を示す
構成図である。FIG. 2 is a configuration diagram showing an example of a conventional floating sampler.
1 醗酵槽 2 プロセス液体(醗酵液) 10 ガス採集容器 11 重り 12 シール部材 13 第1チューブ 14 第2チューブ 17 キャリアガス送出部 18 圧力調節弁 19 圧力計 20 流量調節部 21 ニードル弁 22 流量計 25 圧力計 DESCRIPTION OF SYMBOLS 1 Fermenter 2 Process liquid (fermentation liquid) 10 Gas collection container 11 Weight 12 Sealing member 13 1st tube 14 2nd tube 17 Carrier gas delivery part 18 Pressure control valve 19 Pressure gauge 20 Flow rate control part 21 Needle valve 22 Flow meter 25 Pressure gauge
Claims (1)
形成されたガス採集容器と,該容器中に配置された不活
性部材からなる重りと,前記容器中に一端が挿入され外
周が気密に固定された少なくとも2本のチューブからな
り,前記容器をプロセス液体に浸漬するとともに前記チ
ューブの一方の他端から前記容器内にキャリアガスを導
入し,前記チューブの他方の他端を分析計側に接続した
ことを特徴とするフローティング・サンプラ。1. A gas collection container formed of a member that allows gas to permeate therethrough and a liquid that does not permeate, a weight composed of an inert member disposed in the container, and one end inserted into the container to hermetically seal the outer periphery. At least two tubes fixed to the container, the container is immersed in a process liquid, a carrier gas is introduced into the container from one end of the tube, and the other end of the tube is connected to the analyzer side. A floating sampler characterized by being connected to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23188692A JPH0682433A (en) | 1992-08-31 | 1992-08-31 | Floating sampler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23188692A JPH0682433A (en) | 1992-08-31 | 1992-08-31 | Floating sampler |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0682433A true JPH0682433A (en) | 1994-03-22 |
Family
ID=16930574
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23188692A Pending JPH0682433A (en) | 1992-08-31 | 1992-08-31 | Floating sampler |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0682433A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8650978B2 (en) | 2010-01-15 | 2014-02-18 | Thk Co., Ltd. | Linear actuator provided with dust-proof mechanism |
-
1992
- 1992-08-31 JP JP23188692A patent/JPH0682433A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8650978B2 (en) | 2010-01-15 | 2014-02-18 | Thk Co., Ltd. | Linear actuator provided with dust-proof mechanism |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA1160859A (en) | Method of and apparatus for measuring concentration of gas in a liquid | |
US8447537B2 (en) | Methods and apparatus for determining the permeability and diffusivity of a porous solid | |
US3673853A (en) | Gas content of liquid determination | |
CN106574918B (en) | Method and system for extracting a gas or gas mixture from a liquid for dissolved gas or gas mixture analysis | |
JP3025015B2 (en) | Fluid medium analyzer | |
JPH03502891A (en) | Bioreactors and equipment for culturing animal cells | |
DE69627492D1 (en) | METHOD FOR CORRECTING A LIQUID DELIVERY ERROR AND LIQUID DELIVERY DEVICE | |
Call | Soil fumigation. V.—Diffusion of ethylene dibromide through soils | |
Schnabel et al. | Removal of volatile organic components (VOCs) from water by pervaporation: separation improvement by Dean vortices | |
JPS59131146A (en) | Method and device for monitoring concentration of gas in liquid | |
Schult et al. | Techniques for measurement of water vapor sorption and permeation in polymer films | |
US5616828A (en) | Apparatus and method for testing hydrophobic filters | |
EP0571487A1 (en) | Automated bubble trap | |
JPH0682433A (en) | Floating sampler | |
JPH0151778B2 (en) | ||
US20030119201A1 (en) | Method for determination of product and substrate concentrations in a medium | |
US20040029170A1 (en) | Method and device for the determination of analyte concentrations | |
US3940993A (en) | Proportional fluid sampling device | |
Ho | Effect of sampling variables on recovery of volatile organics in water | |
KR20230125043A (en) | Apparatus and method for continuously testing the gas permeability coefficient of unsaturated soil under varying suction power | |
JPH06273309A (en) | Gas permeability measuring equipment for resin film | |
JPH08108061A (en) | Method for adjusting gaseous mixture composition and method for supplying culture solution using the gaseous mixture | |
US20040250869A1 (en) | Device and method for filling of hydraulic pressure measurement mechanisms | |
CA2500737A1 (en) | Device and method for extracting liquid samples | |
JPH0463335B2 (en) |