JP3453640B2 - Gas-liquid separator with wet steam wetness control - Google Patents

Gas-liquid separator with wet steam wetness control

Info

Publication number
JP3453640B2
JP3453640B2 JP24700494A JP24700494A JP3453640B2 JP 3453640 B2 JP3453640 B2 JP 3453640B2 JP 24700494 A JP24700494 A JP 24700494A JP 24700494 A JP24700494 A JP 24700494A JP 3453640 B2 JP3453640 B2 JP 3453640B2
Authority
JP
Japan
Prior art keywords
gas
liquid
steam
wet steam
liquid separation
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 - Fee Related
Application number
JP24700494A
Other languages
Japanese (ja)
Other versions
JPH0886402A (en
Inventor
守 永瀬
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tlv Co Ltd
Original Assignee
Tlv Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tlv Co Ltd filed Critical Tlv Co Ltd
Priority to JP24700494A priority Critical patent/JP3453640B2/en
Publication of JPH0886402A publication Critical patent/JPH0886402A/en
Application granted granted Critical
Publication of JP3453640B2 publication Critical patent/JP3453640B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】本発明は各種工場や生産プラント
で用いられる蒸気使用装置に供給される湿り蒸気の湿り
度を調節できる機能を備えた気液分離器に関する。 【0002】蒸気は工場やプラントで生産用の熱源とし
て多用されている。蒸気は通常ボイラ―で発生させてそ
れぞれの蒸気使用装置に管を介して送られるが、輸送途
中において放熱等によって熱を奪われ、100パ―セン
トの乾き蒸気ではなく、いくらかの、一般的には数パ―
セントの、湿り度を有している。湿り飽和蒸気1キログ
ラム中に含まれる液体の質量が蒸気の湿り度であり、湿
り度が高いと蒸気中に含まれる水滴の量が多くなり、被
加熱物を均一に加熱することができなくなったり、食品
や薬品等の場合には水損傷を起こしたり、蒸気使用装置
に錆や腐食を生じたり、さらに液体量が増えるとウォ―
タハンマ現象を起こして装置を損傷することがあり、湿
り蒸気の湿り度は厳重に管理されなければならない。 【0003】 【従来技術】そこで従来は、蒸気使用装置の直前に気液
分離器を配置し、水分を蒸気から分離して系外に排除し
ていた。気液分離器としては、気液分離室で遠心力を利
用して気液を分離するものや、気液混合液を衝突板に衝
突させ液体をその衝突板に沿わせて滴下させることによ
り分離するものや、フィルタ―や濾紙等を用いて濾過す
ることにより分離するものが用いられていた。 【0004】 【本発明が解決しようとする課題】上記従来の気液分離
器を配しただけのものでは、蒸気の湿り度が低くなり過
ぎて、一部の繊維や化学製品の加熱の場合には、対象製
品にこげ等の熱損傷を生じる問題があった。従って本発
明の技術的課題は、湿り蒸気の湿り度を調節できる湿り
度調節機能を備えた気液分離器を提供することである。 【0005】 【課題を解決するための手段】本発明の湿り蒸気の湿り
度調節機能を備えた気液分離器の構成は次の通りであ
る。分離器ケ―シングで入口と気液分離室と出口を順次
形成し、気液分離室に気液分離部材を配置し、気液分離
室の下方に連通して液溜め室を設け、出口に設けた絞り
部と液溜め室の液中を連結管で連結すると共に連結管に
流量調節弁を配置したことを特徴とするものである。 【0006】 【作用】気液分離器の入口から流入した湿り蒸気は、気
液分離室において気液分離部材で遠心力や衝突や濾過等
により気液が分離される。分離した水分は下方の液溜め
室に流下し、水分が分離された蒸気は絞り部を通して出
口に至る。蒸気が出口に設けた絞り部を高速で通過する
ときに液溜め室の水分が連結管を介して吸い上げられ再
び蒸気に混合される。連結管に配置した流量調節弁の開
度を調節して再び蒸気に混合される水分量を調節するこ
とにより、蒸気使用装置に供給される湿り蒸気の湿り度
を調節することができる。 【0007】 【実施例】次に、図1に示す実施例を説明する。分離器
ケ―シング1で入口2と気液分離室3と出口4を形成
し、気液分離室3に気液分離部材5を配置する。気液分
離部材5は、二重の円筒部材6の間に形成される環状空
間7をスクリ―ン8を介して入口2と連通し、環状空間
7に入口2からの流体を旋回する旋回羽根9を設けると
共に、内側の円筒部材の下端をすそ広がりの形状にして
水切り部10としたものである。内側の円筒部材の内側
を介して出口4が連通する。出口4には絞り部11を形
成する。 【0008】水切り部10の下方に液溜め室12を連通
し、内部にフロ―ト弁13を自由状態で配置する。フロ
―ト弁13の下部に弁口14を貫通した弁座部材15を
取り付ける。弁口14は液体排出孔16により系外と連
通する。フロ―ト弁13の外周に、フロ―ト弁13の動
揺を防止するためのフロ―トカバ―17を設け、フロ―
トカバ―17上部には貫通孔18を設ける。 【0009】一端が絞り部11内に開口し他端が液溜め
室12の液中に開口する連結管19を設ける。連結管1
9に流量調節弁20を介在させる。連結管19の絞り部
11側開口は水分を噴霧状態で注入できるノズル形状と
することが望ましい。 【0010】次に作用を説明する。入口2から流入して
きた湿り蒸気はスクリ―ン8を通過して気液分離室3に
至る。環状空間7の旋回羽根9により旋回され、質量の
大きな水分は遠心力により外側に振り出され、質量の小
さな蒸気は環状空間7の内側を旋回することにより気液
が分離される。外側に振り出された水分はケ―シング内
壁を伝って液溜め室12内に流下して溜る。吃水線21
以上の水分が溜るとフロ―ト弁13が浮力により浮上し
て弁口14を開口することにより水分は系外に排除され
る。 【0011】水分を分離された蒸気は、水切り部10の
下端から内側の円筒部材の内周に至り、絞り部11を通
過するときに連結管19から液溜め室12の水分を吸い
上げ、出口4から流出する。流量調節弁20の開度を調
節することにより、出口4から流出する湿り蒸気の湿り
度を所望の湿り度に調節することができる。 【0012】 【発明の効果】本発明によれば、流量調節弁の開度を調
節することにより、湿り蒸気の湿り度を調節することが
でき、生産物の損傷等を防止することができる。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas-liquid separator having a function of adjusting the wetness of wet steam supplied to a steam-using device used in various factories and production plants. About the vessel. [0002] Steam is frequently used in factories and plants as a heat source for production. Steam is usually generated in a boiler and sent to each steam-using device via a pipe, but during transportation, heat is taken away by heat radiation and the like. Is a few
Cents of wetness. The mass of the liquid contained in 1 kilogram of wet saturated steam is the wetness of the steam. If the wetness is high, the amount of water droplets contained in the steam will increase, making it impossible to heat the object to be heated uniformly. In the case of food, medicine, etc., water damage may occur, rust or corrosion may occur on equipment that uses steam, or water may increase if the amount of liquid increases.
The equipment may be damaged due to the hammer phenomenon, and the wetness of the wet steam must be strictly controlled. [0003] Conventionally, a gas-liquid separator has been conventionally arranged immediately before a steam-using device to separate moisture from steam and remove it from the system. Gas-liquid separators use a centrifugal force to separate gas and liquid in a gas-liquid separation chamber, or separate by mixing a gas-liquid mixture with a collision plate and allowing the liquid to drip along the collision plate. And those separated by filtration using a filter or filter paper have been used. [0004] In the case where only the above-mentioned conventional gas-liquid separator is provided, the wetness of steam becomes too low, so that heating of some fibers or chemical products is difficult. However, there is a problem that the target product causes heat damage such as burns. Therefore, a technical problem of the present invention is to provide a gas-liquid separator having a wetness adjusting function capable of adjusting the wetness of wet steam. [0005] The structure of the gas-liquid separator having the function of adjusting the wetness of wet steam according to the present invention is as follows. An inlet, a gas-liquid separation chamber, and an outlet are sequentially formed by separator casing, a gas-liquid separation member is arranged in the gas-liquid separation chamber, a liquid storage chamber is provided below the gas-liquid separation chamber, and a liquid storage chamber is provided. The provided throttle section is connected to the liquid in the liquid storage chamber by a connecting pipe, and a flow control valve is arranged in the connecting pipe. The wet steam flowing from the inlet of the gas-liquid separator is separated into gas and liquid by a gas-liquid separation member in a gas-liquid separation chamber by centrifugal force, collision, filtration, and the like. The separated moisture flows down to the lower liquid storage chamber, and the vapor from which the moisture has been separated reaches the outlet through the throttle. When the steam passes through the throttle provided at the outlet at a high speed, the water in the liquid storage chamber is sucked up through the connecting pipe and mixed with the steam again. By adjusting the opening of the flow control valve disposed in the connecting pipe to adjust the amount of water mixed with the steam again, the wetness of the wet steam supplied to the steam using device can be adjusted. Next, an embodiment shown in FIG. 1 will be described. The inlet 2, the gas-liquid separation chamber 3 and the outlet 4 are formed by the separator casing 1, and the gas-liquid separation member 5 is disposed in the gas-liquid separation chamber 3. The gas-liquid separation member 5 communicates an annular space 7 formed between the double cylindrical members 6 with the inlet 2 via a screen 8, and swirl vanes for swirling the fluid from the inlet 2 into the annular space 7. 9 is provided, and the lower end of the inner cylindrical member is formed in a flared shape to form a drainer 10. The outlet 4 communicates through the inside of the inner cylindrical member. A throttle 11 is formed at the outlet 4. [0008] A liquid reservoir chamber 12 is communicated below the draining section 10 and a float valve 13 is disposed in a free state therein. A valve seat member 15 penetrating through a valve port 14 is attached to a lower portion of the float valve 13. The valve port 14 communicates with the outside of the system through a liquid discharge hole 16. On the outer periphery of the float valve 13, a float cover 17 for preventing the float valve 13 from oscillating is provided.
A through hole 18 is provided in the upper part of the cover 17. A connection pipe 19 is provided, one end of which opens into the throttle section 11 and the other end of which opens into the liquid in the liquid reservoir chamber 12. Connecting pipe 1
9 is provided with a flow control valve 20. It is desirable that the opening of the connecting pipe 19 on the throttle unit 11 side be a nozzle shape capable of injecting water in a spray state. Next, the operation will be described. The wet steam flowing from the inlet 2 passes through the screen 8 and reaches the gas-liquid separation chamber 3. The water is swirled by the swirling blades 9 of the annular space 7, the water having a large mass is squirted outward by centrifugal force, and the vapor having a small mass is swirled inside the annular space 7 to separate gas and liquid. The water spouted outward travels along the inner wall of the casing and flows down into the liquid storage chamber 12 to be stored. Draft line 21
When the above-mentioned moisture accumulates, the float valve 13 floats by buoyancy and opens the valve port 14, whereby the moisture is discharged out of the system. The steam from which the water has been separated reaches the inner periphery of the inner cylindrical member from the lower end of the water draining section 10, sucks the water in the liquid storage chamber 12 from the connecting pipe 19 when passing through the throttle section 11, and Spill out of. By adjusting the opening of the flow control valve 20, the wetness of the wet steam flowing out of the outlet 4 can be adjusted to a desired wetness. According to the present invention, by adjusting the opening of the flow control valve, the wetness of the wet steam can be adjusted, and damage to the product can be prevented.

【図面の簡単な説明】 【図1】本発明の湿り蒸気の湿り度調節機能を備えた気
液分離器の断面図である。 【符号の説明】 1 分離器ケ―シング 2 入口 3 気液分離室 4 出口 5 気液分離部材 11 絞り部 12 液溜め室 19 連結管 20 流量調節弁
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a cross-sectional view of a gas-liquid separator having a function of adjusting the wetness of wet steam according to the present invention. [Description of Signs] 1 Separator casing 2 Inlet 3 Gas-liquid separation chamber 4 Outlet 5 Gas-liquid separation member 11 Throttle section 12 Liquid storage chamber 19 Connecting pipe 20 Flow control valve

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F22B 37/26 F22G 5/12 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int. Cl. 7 , DB name) F22B 37/26 F22G 5/12

Claims (1)

(57)【特許請求の範囲】 【請求項1】 分離器ケ―シングで入口と気液分離室と
出口を順次形成し、気液分離室に気液分離部材を配置
し、気液分離室の下方に連通して液溜め室を設け、出口
に設けた絞り部と液溜め室の液中を連結管で連結すると
共に連結管に流量調節弁を配置したことを特徴とする湿
り蒸気の湿り度調節機能を備えた気液分離器。
(57) [Claims 1] An inlet, a gas-liquid separation chamber, and an outlet are sequentially formed by separator casing, and a gas-liquid separation member is disposed in the gas-liquid separation chamber. Characterized in that a liquid storage chamber is provided in communication with the lower part of the chamber, and a restrictor provided at the outlet and the liquid in the liquid storage chamber are connected by a connecting pipe, and a flow control valve is disposed in the connecting pipe. Gas-liquid separator with degree adjustment function.
JP24700494A 1994-09-14 1994-09-14 Gas-liquid separator with wet steam wetness control Expired - Fee Related JP3453640B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24700494A JP3453640B2 (en) 1994-09-14 1994-09-14 Gas-liquid separator with wet steam wetness control

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24700494A JP3453640B2 (en) 1994-09-14 1994-09-14 Gas-liquid separator with wet steam wetness control

Publications (2)

Publication Number Publication Date
JPH0886402A JPH0886402A (en) 1996-04-02
JP3453640B2 true JP3453640B2 (en) 2003-10-06

Family

ID=17156957

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24700494A Expired - Fee Related JP3453640B2 (en) 1994-09-14 1994-09-14 Gas-liquid separator with wet steam wetness control

Country Status (1)

Country Link
JP (1) JP3453640B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4657422B2 (en) * 2000-07-14 2011-03-23 株式会社テイエルブイ Gas-liquid separator
JP4489377B2 (en) * 2003-06-13 2010-06-23 株式会社テイエルブイ Gas-liquid separator with drainage valve
JP4489376B2 (en) * 2003-06-13 2010-06-23 株式会社テイエルブイ Gas-liquid separator
JP4684542B2 (en) * 2003-07-15 2011-05-18 株式会社テイエルブイ Gas-liquid separator with drainage valve
JP2006167577A (en) * 2004-12-15 2006-06-29 Tlv Co Ltd Gas-liquid separator

Also Published As

Publication number Publication date
JPH0886402A (en) 1996-04-02

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