JPS58180223A - Gas separating device - Google Patents
Gas separating deviceInfo
- Publication number
- JPS58180223A JPS58180223A JP6403282A JP6403282A JPS58180223A JP S58180223 A JPS58180223 A JP S58180223A JP 6403282 A JP6403282 A JP 6403282A JP 6403282 A JP6403282 A JP 6403282A JP S58180223 A JPS58180223 A JP S58180223A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- piping
- separation
- stage
- pipings
- 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
- Separation Of Gases By Adsorption (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は重ガス成分と軽ガス成分とを含む混合ガスを各
成分ガスシニ分離する分離要素を複数台東合横密配置に
収容したチェンバーをカスケード方式に接続したガス分
離装置に関する。[Detailed Description of the Invention] [Technical Field of the Invention] The present invention utilizes a cascade system in which a chamber containing a plurality of separation elements for separating a mixed gas containing a heavy gas component and a light gas component into each component gas is housed in a horizontally packed arrangement. Relating to a gas separation device connected to.
カスケード方式で接続されたガス分離装置では、その分
離段および配管内のガスを完全に排出する場合、かなり
の長時間を要する欠点がある。Gas separation devices connected in a cascade system have the disadvantage that it takes a considerable amount of time to completely exhaust the gas in the separation stages and piping.
本発明は上記欠点を除去するためになされたもので、チ
ェンバー同志を配管接続するだけで、ガス排出すなわち
排気に要する輪間を大巾に短縮することを可能にしたガ
ス分離装置を提供することにある。The present invention has been made in order to eliminate the above-mentioned drawbacks, and provides a gas separation device that makes it possible to greatly shorten the distance between the rings required for gas discharge, that is, by simply connecting the chambers together with piping. It is in.
すなわち、本発明は分離カスケードの排気配管として、
分離カスケードの構成要素であるチェンバー自身を排気
用配管に兼用させるため分離段にてチェンバーを直列に
接続しかつ分離段自身も直列に配管接続し排気性能を向
上させることを特徴とするガス分離装置である。That is, the present invention provides exhaust piping for a separation cascade.
A gas separation device characterized in that the chambers, which are constituent elements of a separation cascade, are connected in series at the separation stage so that the chambers themselves are also used as exhaust piping, and the separation stage itself is also connected with piping in series to improve exhaust performance. It is.
以下、図面について本発明の一実施例を説明する。 An embodiment of the present invention will be described below with reference to the drawings.
図において、符号1は複数の分離要素を収容するチェン
バーで、このチェンバー1は分離要素をまとめた部分す
なわち分離室2と分離要素間の空間6とからなっている
。In the figure, reference numeral 1 denotes a chamber that accommodates a plurality of separation elements, and this chamber 1 consists of a portion where the separation elements are grouped together, that is, a separation chamber 2 and a space 6 between the separation elements.
そして各チェンバー1を並列にプロセス用ヘッダー配管
4にて接続する。Then, each chamber 1 is connected in parallel with a process header piping 4.
なお、図中符号M、 、 M、、 M、、・・・は分離
段(M段)であって、N、、N、、N、、・・・は他の
分離段(N段)、またL段等を示す。In addition, the symbols M, , M,, M, ... in the figure are separation stages (M stages), and N,, N,, N, ... are other separation stages (N stages), It also shows the L stage, etc.
各分離段は、公知のようにプロヤス用ヘッダー配管4,
5で接続されて分離カスケードが構成される。As is well known, each separation stage includes header piping 4 for Proyas,
5 to form a separate cascade.
しかして、分離段を接続するプロセス用ヘッダー配管6
はそれぞれ2本より構成されM段に着目すれば、上段の
N段より1本を用いてガスが供給され、他のもう1本は
自段の出力用配管となる。Therefore, the process header piping 6 that connects the separation stage
are each composed of two pipes, and focusing on the M stage, one pipe is used to supply gas from the upper N stage, and the other pipe serves as the output pipe of the own stage.
そして、下段のL段とは2本からなる接続配管5のうち
1本を用いてガスがL段より供給され他の1本が自段の
出力用配管となる。Gas is supplied from the L stage to the lower L stage using one of the two connecting pipes 5, and the other pipe serves as the output pipe of the own stage.
それぞれの段においては、チェンバー1を並列接続する
ために〜ラダー配管4によって接続されるようになって
いる。Each stage is connected by ladder piping 4 in order to connect the chambers 1 in parallel.
すべての分離段はチェンバー1の空間3に排気用ヘッダ
ー配管6によって接続され、かつり、M。All separation stages are connected to the space 3 of the chamber 1 by exhaust header piping 6, and are connected to the space 3 of the chamber 1.
Nの段方向には排気用ヘッダー配管7に上って膜内並列
方向段方向に直列に配管接続している。In the direction of the N stage, it goes up to the exhaust header piping 7 and is connected to the pipe in series in the direction of the parallel direction in the membrane.
以上のようなすべてのチェンバー1の接続関係の構成に
おいてすべての分離段およびプロセスヘッダー配管4,
5から排気するには排気用ヘッダー配管6,7によって
分離段とヘッダが前述のような連通関係で接続されてい
るので例えば図示のA点より排気すればガスはすべての
チェンバー1の内部を経由に流れることになる。In all the connection configurations of the chamber 1 as described above, all separation stages and process header piping 4,
In order to exhaust gas from chamber 5, the separation stage and the header are connected in the above-mentioned communication relationship by exhaust header piping 6 and 7, so if the gas is exhausted from point A shown in the figure, for example, the gas will pass through the inside of all chambers 1. It will flow to
また本発明め構成においては図示の破線の如く弁8,9
を介してチェンバーを接続しても良い。In addition, in the configuration of the present invention, the valves 8 and 9 are as shown by the broken lines in the figure.
You may also connect the chamber via.
この場合は弁8,9の開閉によって種々の運転モードに
対応できることとなるが、コスト高となることから必ず
しも設置しなくても良いのである。In this case, various operation modes can be accommodated by opening and closing the valves 8 and 9, but this does not necessarily have to be installed because of the high cost.
特に役向における弁9を設置せず、段接続用弁8を設置
することが考えられる。In particular, it is conceivable to install the stage connection valve 8 without installing the valve 9 for the role.
段接続用弁8は通常段同志等圧であるので、通常の運転
時ガスの流れは生じていないが微小量の流れを防止する
役目を持たすことができる。Since the stage connection valves 8 are normally at the same pressure between the stages, they can have the role of preventing a small amount of gas flow even though no gas flow occurs during normal operation.
以上説明したように本発明によればチェンバー1内に分
離要素を複数台収容するために内部に排気しなければな
らない大きな空間3が生じても、チェンバー1の分離室
2を経由することなく、直接排気できるので分離要素内
の排気を迅速に行なうことができる。As explained above, according to the present invention, even if a large space 3 is created in the chamber 1 that must be evacuated in order to accommodate a plurality of separation elements, the air can be evacuated without going through the separation chamber 2 of the chamber 1. Since the separation element can be directly evacuated, the separation element can be evacuated quickly.
図は本発明に係るガス分離装置の一実施例を示す配管系
統図である。
丁 ・・・・・・ チェンバー
2 ・・・−・分離室
3 ・・・・・・分離要素の空間
4.5・・・プロセス用ヘッダー配管
6.7・・・排気用〜ブダー配管
8.9・・・弁
(7317)代理人弁理士 則 近 憲 佑(は力弓名
)The figure is a piping system diagram showing an embodiment of the gas separation device according to the present invention. Chamber 2 Separation chamber 3 Separation element space 4.5 Process header piping 6.7 Exhaust to budder piping 8. 9...Ben (7317) Representative Patent Attorney Kensuke Chika (his name is Rikikyu)
Claims (1)
置して収容した複数のチェンバーと、これら複数のチェ
ンバーを並列接続した分離段ユニットと、この分離段ユ
ニットを接続した複数段のカスケードとを具備したガス
分離装置において、前記分離段ユニット内で並列接続さ
れたチェンバー同志を直列に配管接続し、かつ分離段ユ
ニット同志をその構成要素であるチェンバーを介して直
列に配管接続し、しかも前記チェンバーに収容された分
離要素間の空間を排気できるようζミ構成したことを特
徴とするガス分離装置。 2、複数のチェンバー間の接続に弁を介して配管接続し
てなることを特徴とする特許請求の範囲第1項記載のガ
ス分離装置。[Claims] 1. A plurality of separation elements, a plurality of chambers housing these separation elements in a dense arrangement, a separation stage unit in which these plurality of chambers are connected in parallel, and a connection of this separation stage unit. In the gas separation apparatus, the chambers connected in parallel within the separation stage unit are connected in series via piping, and the separation stage units are connected in series through the chambers that are their constituent elements. A gas separation apparatus characterized in that the gas separation apparatus is connected to piping and configured in a ζ-mi configuration so that the space between the separation elements housed in the chamber can be evacuated. 2. The gas separation device according to claim 1, characterized in that the plurality of chambers are connected by piping via valves.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6403282A JPS58180223A (en) | 1982-04-19 | 1982-04-19 | Gas separating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6403282A JPS58180223A (en) | 1982-04-19 | 1982-04-19 | Gas separating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58180223A true JPS58180223A (en) | 1983-10-21 |
Family
ID=13246374
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6403282A Pending JPS58180223A (en) | 1982-04-19 | 1982-04-19 | Gas separating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58180223A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998005196A1 (en) | 1996-08-01 | 1998-02-12 | M & M Laboratory Co., Ltd. | Water-holding carrier for plants |
US6388000B1 (en) | 1992-06-10 | 2002-05-14 | Nippon Shokubai Co., Ltd. | Method for production of hydrophilic resin |
-
1982
- 1982-04-19 JP JP6403282A patent/JPS58180223A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6388000B1 (en) | 1992-06-10 | 2002-05-14 | Nippon Shokubai Co., Ltd. | Method for production of hydrophilic resin |
US6998447B2 (en) | 1992-06-10 | 2006-02-14 | Nippon Shokubai Co., Ltd. | Method for production of hydrophilic resin |
US7078458B2 (en) | 1992-06-10 | 2006-07-18 | Nippon Shokubai Co., Ltd. | Method for production of hydrophilic resin |
WO1998005196A1 (en) | 1996-08-01 | 1998-02-12 | M & M Laboratory Co., Ltd. | Water-holding carrier for plants |
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