JP2519396Y2 - Structure of brackish water separator of multi-tube once-through boiler - Google Patents

Structure of brackish water separator of multi-tube once-through boiler

Info

Publication number
JP2519396Y2
JP2519396Y2 JP2339191U JP2339191U JP2519396Y2 JP 2519396 Y2 JP2519396 Y2 JP 2519396Y2 JP 2339191 U JP2339191 U JP 2339191U JP 2339191 U JP2339191 U JP 2339191U JP 2519396 Y2 JP2519396 Y2 JP 2519396Y2
Authority
JP
Japan
Prior art keywords
water
chamber
water separator
boiler
brackish
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
JP2339191U
Other languages
Japanese (ja)
Other versions
JPH04108106U (en
Inventor
野村洋一
Original Assignee
株式会社サムソン
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 株式会社サムソン filed Critical 株式会社サムソン
Priority to JP2339191U priority Critical patent/JP2519396Y2/en
Publication of JPH04108106U publication Critical patent/JPH04108106U/en
Application granted granted Critical
Publication of JP2519396Y2 publication Critical patent/JP2519396Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】本考案は多管式貫流ボイラの縦型
の汽水器の構造に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a structure of a vertical steam generator of a multi-tube once-through boiler.

【従来の技術】[Prior art]

【0002】多管式貫流ボイラでは、給水ポンプからの
給水は、直接またはブロー水と熱交換した後、比較的低
温のままでボイラ本体へ給水されるのが通例であるた
め、給水中の溶存酸素によりボイラ本体の腐食が進行す
るという問題点がある。従来から給水中の溶存酸素を減
少させるために、給水ポンプからの給水を汽水分離器に
供給して汽水分離器内の高温度の缶水と混合させた後、
ボイラへ供給するようにした給水方法が知られている
が、従来の汽水分離器においてこの給水方法を採用した
場合には、汽水分離器内で分離された缶水が給水により
薄められるため、高濃度の濃縮水をブローすることが出
来ず、ボイラ内全体の缶水濃度を規定濃度以下に低下さ
せるために、多量のブローを必用とするいう問題点があ
った。
In a multi-tube once-through boiler, the water supplied from a water supply pump is usually supplied to the boiler body at a relatively low temperature directly or after heat exchange with blow water. There is a problem that oxygen causes corrosion of the boiler body. Conventionally, in order to reduce the dissolved oxygen in the feedwater, after the feedwater from the feedwater pump is supplied to the brackish water separator and mixed with the high temperature canned water in the brackish water separator,
A water supply method that supplies water to a boiler is known. However, when this water supply method is used in a conventional brackish water separator, the can water separated in the brackish water separator is diluted by the water supply, so that There was a problem that it was impossible to blow concentrated water having a concentration, and a large amount of blowing was necessary in order to reduce the concentration of can water in the entire boiler to below the specified concentration.

【考案が解決しようとする課題】[Problems to be solved by the device]

【0003】本考案の目的は汽水分離器内において、補
給水中に含まれる溶存酸素を低減し、かつ、濃縮度の高
い缶水をブローすることである。
An object of the present invention is to reduce dissolved oxygen contained in makeup water and blow can water having a high degree of concentration in a brackish water separator.

【課題を解決するための手段】[Means for Solving the Problems]

【0004】本考案においては、サイクロン式の縦型汽
水分離器の内部を仕切板並びに案内板を設け、濃縮水室
と脱気室に分けることにより、上述の課題を解決した。
脱気室に給水口を設け、高温分離水と給水を混合・攪拌
させることにより、給水中に含まれる溶存酸素を分離さ
せる。また、高濃縮度の分離水を濃縮水室に溜め、給水
によって薄められることなく、間欠的にブローさせるこ
とにより、ブロー量を低減しブロー熱損失を低減する。
In the present invention, the above-mentioned problems are solved by providing a partition plate and a guide plate inside the cyclone type vertical brackish water separator to divide it into a concentrated water chamber and a deaeration chamber.
A water supply port is provided in the degassing chamber, and high-temperature separated water and feed water are mixed and stirred to separate dissolved oxygen contained in the feed water. Further, the separated water having a high degree of concentration is stored in the concentrated water chamber, and is intermittently blown without being diluted by the water supply, thereby reducing the blow amount and the blow heat loss.

【作用】[Action]

【0005】ボイラ缶内で発生した蒸気は、蒸気入口管
より汽水分離器内へ旋回しながら入るため、遠心力によ
り乾き蒸気と水に分離する。この分離水は濃縮水室に留
められ、給水で薄められることなく濃縮水ブロー口より
間欠的に排水される。残りの分離水は汽水分離器胴内壁
と案内板との間隙を通過して、または濃縮水室をオーバ
ーフローして脱気室に送られる。一方、給水は給水配管
を通って脱気室からあふれた分離水と混合し、ボイラ缶
内へ供給される。給水中に含まれる溶存酸素は高温分離
水と混合されることにより分離され、蒸気出口より排出
される。
The steam generated in the boiler can swirls into the brackish water separator through the steam inlet pipe, and is separated into dry steam and water by centrifugal force. This separated water is retained in the concentrated water chamber and is intermittently discharged from the concentrated water blow port without being diluted by the water supply. The remaining separated water passes through the gap between the inner wall of the brackish water separator barrel and the guide plate, or overflows the concentrated water chamber and is sent to the deaeration chamber. On the other hand, the water supply is mixed with the separated water overflowing from the degassing chamber through the water supply pipe and supplied into the boiler can. The dissolved oxygen contained in the feed water is separated by being mixed with the high temperature separated water and discharged from the steam outlet.

【実施例】【Example】

【0006】本考案の一実施例を図を用いて説明する。
汽水分離器は縦長の円筒柱形の胴の上下に半球状もしく
は皿状の鏡板を取り付けた容器に、図1に示すように上
部に蒸気出口管2、下部に環水管3を設置する。さら
に、分離水滴が胴内壁を伝わって蒸気出口管2へ混入す
るのを防ぐため、汽水分離器内に蒸気出口管2の一部を
突出し、図1に示すようにスカート12を設置する。汽
水分離器1の胴体部分にボイラ本体の上部管寄せからの
蒸気入口管4を円筒柱の接線方向に図2に示すように設
置する。
An embodiment of the present invention will be described with reference to the drawings.
In the brackish water separator, a vertically long cylindrical columnar cylinder is provided with hemispherical or dish-shaped end plates above and below, and a steam outlet pipe 2 is installed in the upper part and a water ring pipe 3 is installed in the lower part as shown in FIG. Further, in order to prevent separated water droplets from being mixed with the steam outlet pipe 2 along the inner wall of the body, a part of the steam outlet pipe 2 is projected in the brackish water separator, and the skirt 12 is installed as shown in FIG. The steam inlet pipe 4 from the upper head of the boiler body is installed in the body of the brackish water separator 1 in the tangential direction of the cylindrical column as shown in FIG.

【0007】汽水分離器内の蒸気入口管4より下部に仕
切板5を設ける。仕切板5は胴内壁に溶接固定し、胴下
部を濃縮水室6と脱気室7に2分する。案内板11は仕
切板5の上部に接続して濃縮水室側に傾きをもって設け
る。仕切板5の下部に濃縮水槽6から脱気室7へ連通す
る小径の穴13を設ける。
A partition plate 5 is provided below the steam inlet pipe 4 in the brackish water separator. The partition plate 5 is fixed to the inner wall of the body by welding, and the lower part of the body is divided into a concentrated water chamber 6 and a deaeration chamber 7. The guide plate 11 is connected to the upper part of the partition plate 5 and is provided with an inclination toward the concentrated water chamber side. A small-diameter hole 13 that communicates from the concentrated water tank 6 to the degassing chamber 7 is provided below the partition plate 5.

【0008】濃縮水室6の下部側胴部に濃縮水ブロー口
9と缶水濃度センサー取付口8を設ける。脱気室7の側
胴部に給水管10を円筒柱の接線方向に図2に示すよう
に取り付ける。
A concentrated water blow port 9 and a can water concentration sensor mounting port 8 are provided on the lower body of the concentrated water chamber 6. The water supply pipe 10 is attached to the side body of the degassing chamber 7 in the tangential direction of the cylindrical column as shown in FIG.

【0009】[0009]

【考案の効果】汽水分離器で分離された分離水が濃縮水
室で留められ、補給水で薄められることなく、高濃度の
缶水のブローが可能となるため、濃縮水ブロー量の低減
がはかれる。汽水分離器の脱気室においては、給水を分
離水と混合させる事により、給水中の溶存酸素の低減が
可能となるため、缶内腐食の低減と同時に薬注量の低減
がはかれる。
[Advantage of the Invention] Since the separated water separated by the brackish water separator is retained in the concentrated water chamber and the concentrated water can be blown without being diluted with makeup water, the amount of concentrated water blown can be reduced. Be peeled off. In the degassing chamber of the brackish water separator, mixing the feed water with the separated water makes it possible to reduce the dissolved oxygen in the feed water, which reduces corrosion in the can and at the same time reduces the amount of chemical injection.

【図面の簡単な説明】[Brief description of drawings]

【図1】 縦断面図FIG. 1 is a longitudinal sectional view

【図2】 図1のA−A断面から下観図FIG. 2 is a perspective view from the AA cross section of FIG.

【図3】 図2のB−B断面図3 is a sectional view taken along line BB of FIG.

【符号の説明】[Explanation of symbols]

1 汽水分離器本体 2 蒸気出口管 3 環水管 4 蒸気入口管 5 仕切板 6 濃縮水室 7 脱気室 8 缶水濃縮センサー取付口 9 濃縮水ブロー口 10 給水管 11 案内板 12 スカート 13 穴 1 Brackish water separator body 2 Steam outlet pipe 3 Ring water pipe 4 Steam inlet pipe 5 Partition plate 6 Concentrated water chamber 7 Deaeration chamber 8 Can water concentration sensor mounting port 9 Concentrated water blow port 10 Water supply pipe 11 Guide plate 12 Skirt 13 hole

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of utility model registration request] 【請求項1】上部に蒸気出口管2を、胴部分に胴に対し
て接線方向に蒸気入口管4を、下部に缶体下部へ連絡す
る環水管3を取り付けた汽水分離器において、汽水分離
器内の蒸気入口より下の部分に仕切板5を設け濃縮水室
6と脱気室7を形成し、仕切板上部に接続して分離水を
濃縮水室6へ導く案内板11を設け,濃縮水室に濃縮水
ブロー口9並びに缶水濃縮センサー取付口8を設け、脱
気室に給水管10を設けたことを特長とする汽水分離器
の構造。
1. A brackish water separator in which a steam outlet pipe 2 is attached to an upper portion, a steam inlet pipe 4 is attached to a barrel portion in a tangential direction to the barrel, and a ring water pipe 3 which is connected to a lower portion of a can is attached to a lower portion of the barrel. A partition plate 5 is provided below the steam inlet in the vessel to form a concentrated water chamber 6 and a deaeration chamber 7, and a guide plate 11 is provided which is connected to the upper part of the partition plate to guide the separated water to the concentrated water chamber 6, A structure of a brackish water separator characterized in that a concentrated water blow port 9 and a can water concentration sensor mounting port 8 are provided in the concentrated water chamber, and a water supply pipe 10 is provided in a deaeration chamber.
JP2339191U 1991-02-16 1991-02-16 Structure of brackish water separator of multi-tube once-through boiler Expired - Fee Related JP2519396Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2339191U JP2519396Y2 (en) 1991-02-16 1991-02-16 Structure of brackish water separator of multi-tube once-through boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2339191U JP2519396Y2 (en) 1991-02-16 1991-02-16 Structure of brackish water separator of multi-tube once-through boiler

Publications (2)

Publication Number Publication Date
JPH04108106U JPH04108106U (en) 1992-09-18
JP2519396Y2 true JP2519396Y2 (en) 1996-12-04

Family

ID=31908641

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2339191U Expired - Fee Related JP2519396Y2 (en) 1991-02-16 1991-02-16 Structure of brackish water separator of multi-tube once-through boiler

Country Status (1)

Country Link
JP (1) JP2519396Y2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10220705A (en) * 1997-02-10 1998-08-21 Kawasaki Thermal Eng Co Ltd Method and apparatus for separating concentrated boiler water and suppied water in boiler
JP2002028421A (en) * 2000-07-18 2002-01-29 Samson Co Ltd Centrifugal gas/liquid separator using separation by baffle plate in combination
JP5510788B2 (en) * 2009-10-30 2014-06-04 三浦工業株式会社 Steam separator

Also Published As

Publication number Publication date
JPH04108106U (en) 1992-09-18

Similar Documents

Publication Publication Date Title
JP2519396Y2 (en) Structure of brackish water separator of multi-tube once-through boiler
WO2009068616A1 (en) Degasser
FI875433A0 (en) ANORDNING FOER VAERMEVAEXLING, SPECIELLT MELLAN SYNTESGAS- OCH PANNMATNINGSVATTEN.
JP2008261538A (en) Steam separator and boiler device comprising the same
US4292275A (en) Modular chlorine dioxide generation systems
JPH0621531Y2 (en) Steam separator
JP2004249164A (en) Air-water separator
JPH07187282A (en) Liquid storage tank
JPS6241766B2 (en)
JP2012037175A (en) Deaerator
JPH0726725B2 (en) Steam separator with water inlet and concentrated water blower
JPS5838243Y2 (en) Boiler and deaerator water supply inner pipes
SU1183778A1 (en) Thermal deaerator
JPH025202Y2 (en)
JPH082450Y2 (en) Cylinder block
JPH07124404A (en) Degasifier
SU1386216A1 (en) Evaporator of immersion combustion
CN214344540U (en) Vacuum crystallizer defoaming device for titanium dioxide
SU1305445A1 (en) Jet apparatus
JPH0711291Y2 (en) Water-water separation structure of multi-tube once-through boiler
JPS6143552Y2 (en)
SU1286877A1 (en) Thermal deaerator
CN2297632Y (en) High efficiency film-type deaerator
JPS5916082Y2 (en) water treatment equipment
SU1219869A1 (en) Thermal deaerator

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees