JP2007303627A - Steam eliminator for steam trap - Google Patents
Steam eliminator for steam trap Download PDFInfo
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- JP2007303627A JP2007303627A JP2006134938A JP2006134938A JP2007303627A JP 2007303627 A JP2007303627 A JP 2007303627A JP 2006134938 A JP2006134938 A JP 2006134938A JP 2006134938 A JP2006134938 A JP 2006134938A JP 2007303627 A JP2007303627 A JP 2007303627A
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- steam
- steam trap
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- liquid separation
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本発明は、蒸気トラップの出口から排出される復水の再蒸発に伴うモヤモヤと立ち昇る湯気を防止することのできる蒸気トラップの消湯気器に関する。 The present invention relates to a steam trap water heater capable of preventing smoky and rising steam accompanying re-evaporation of condensate discharged from the outlet of the steam trap.
蒸気トラップの消湯気器は、蒸気トラップの出口に排出管と上下に位置する水溜部を設けて、再蒸発した蒸気を上部の水溜部を通過させて冷却することによって、モヤモヤと立ち昇る再蒸発蒸気の湯気を防止することができるものである。 The steam trap water heater is equipped with a discharge pipe and an upper and lower water reservoir at the outlet of the steam trap, and the re-evaporated steam rises rapidly by passing through the upper water reservoir and cooling it. Steam vapor can be prevented.
この蒸気トラップの消湯気器では、モヤモヤとした湯気を確実に消すために、排出管の上下に数多くの水溜部を設ける必要があり、消湯気器そのものが大型化して高価なものとなってしまう問題点があった。
解決しようとする課題は、復水の再蒸発に伴うモヤモヤとした湯気を確実に目立たなくすることのできる小型で安価な蒸気トラップの消湯気器を提供することである。 The problem to be solved is to provide a small and inexpensive steam trap water heater that can surely obscure the smoky steam accompanying re-evaporation of the condensate.
本発明は、蒸気トラップの出口から大気中へ排出される復水が再蒸発してモヤモヤと立ち昇る湯気を防止すものにおいて、蒸気トラップの出口側に、蒸気は透過させるが液体は透過させない気液分離膜で形成した長尺状の細管を連設して、当該細管内を復水が流下する間に、復水が再蒸発して復水の保有する熱を大気中に放熱することによって、モヤモヤと立ち昇る湯気を目立たなくするものである。 In the present invention, steam that permeates vapor but does not allow liquid to permeate to the outlet side of the steam trap in the condensate discharged from the outlet of the steam trap to the atmosphere to prevent re-evaporation and rise. By connecting a long narrow tube formed of a liquid separation membrane, the condensed water re-evaporates and the heat held by the condensed water is released into the atmosphere while the condensed water flows down in the narrow tube. The steam that rises up and gets wet is inconspicuous.
本発明の蒸気トラップの消湯気器は、蒸気トラップの出口側に取り付けた気液分離膜で形成した長尺状の細管内を、復水が流下する間に、長尺状の細管の全外表面から微少量ごとの復水が再蒸発して細管の細孔を通って大気中へ放散されることによって、復水の保有する熱を大気中へ放熱することにより復水が冷却され、且つ、長尺状の細管の全外表面から微少量ごとの再蒸発蒸気が放散されるために、再蒸発蒸気が一箇所からまとまってモヤモヤと立ち昇るようなことがなく、湯気を目立たなくすることができ、小型で安価な蒸気トラップの消湯気器とすることができる。 The steam trap water heater according to the present invention has a long thin tube formed by a gas-liquid separation membrane attached to the outlet side of the steam trap, while the condensate flows down the entire length of the long thin tube. A small amount of condensate is re-evaporated from the surface and dissipated into the atmosphere through the fine pores of the narrow tube, and the condensate is cooled by dissipating the heat held by the condensate into the atmosphere, and In addition, since the re-evaporated vapor is dissipated every minute from the entire outer surface of the long thin tube, the re-evaporated vapor does not rise together from one place and the steam does not stand out. Therefore, the steam trap can be a small and inexpensive steam trap.
本発明は、気液分離膜で形成した長尺状の細管を用いるものであるが、気液分離膜としては、従来から膜蒸留法などで使用されている疎水性多孔質膜を用いることができ、また、細管の管径や長さなどは、蒸気トラップの出口から排出される復水の量や温度に応じて適宜選定することができる。 In the present invention, a long thin tube formed of a gas-liquid separation membrane is used. As the gas-liquid separation membrane, a hydrophobic porous membrane conventionally used in a membrane distillation method or the like is used. In addition, the diameter and length of the narrow tube can be appropriately selected according to the amount and temperature of the condensate discharged from the outlet of the steam trap.
本実施例においては図1に示すように、入口1と出口2を備えた蒸気トラップ3と、蒸気トラップ3の出口2に連設した複数本の気液分離膜で形成した螺旋状細管4とで蒸気トラップの消湯気器を構成する。 In this embodiment, as shown in FIG. 1, a steam trap 3 having an inlet 1 and an outlet 2, and a spiral tubule 4 formed of a plurality of gas-liquid separation membranes connected to the outlet 2 of the steam trap 3, Construct a steam trap water heater.
蒸気トラップ3の入口1は図示しない蒸気使用装置と接続することにより、蒸気使用装置で蒸気の凝縮した復水と一部蒸気との混合流体が、蒸気トラップ3内に流入する。蒸気トラップ3は、復水を出口2から外部へ排出するが、蒸気は排出することのない自動弁の一種である。 By connecting the inlet 1 of the steam trap 3 to a steam using device (not shown), a mixed fluid of the condensate condensed with the steam and the partial steam flows in the steam trap 3. The steam trap 3 is a kind of automatic valve that discharges condensate from the outlet 2 to the outside, but does not discharge steam.
気液分離膜で形成した長尺状の細管4は、本実施例においてはそれぞれ連続した螺旋状に曲げ加工して取り付ける。この長尺状の細管4の外表面には図示はしていないが、気体としての蒸気は透過するが液体は透過することのない微小な細孔を多数有するものである。また、複数の螺旋状細管4はそれぞれ極力接触しないように配置して、大気中への放熱及び蒸気の放散が阻害されないようにする。 In this embodiment, the long tubules 4 formed of a gas-liquid separation membrane are each bent and attached in a continuous spiral shape. Although not illustrated on the outer surface of the long thin tube 4, it has a large number of minute pores that allow vapor as a gas to pass through but do not allow liquid to pass through. Further, the plurality of spiral capillaries 4 are arranged so as not to contact each other as much as possible so that heat radiation to the atmosphere and vapor diffusion are not hindered.
複数の螺旋状細管4の右端にはL字状の配管部材であるエルボ5を接続する。複数の螺旋状細管4の両端部と、蒸気トラップ3の出口2及びエルボ5の接続部は、溶接又はろう付け等によって気密に接合する。気液分離膜で形成した細管4の総有効内径断面積は、蒸気トラップ3の出口2の内径断面積と、及び、エルボ5の内径断面積と極力等しくなるように選定する。
An
エルボ5の下端部には、小径貫通孔6を設けたオリフィス・プレート7を取り付ける。小径貫通孔6の断面積は、エルボ5の内径断面積よりも小さくして、絞り作用を果たすものである。
An orifice plate 7 provided with a small diameter through
蒸気トラップ3の出口2から排出される復水は高温状態であり、気液分離膜で形成した細管4内を分配されて流下する間に、復水の一部が再度蒸発して細管4外表面の多数の細孔から大気中へ放散されることによってその熱が大気中へ放熱されて復水は冷却される。この場合、大気中へ放散される再蒸発蒸気は、複数の長尺状細管4の外表面全体からそれぞれ分散されて放散されるために、一箇所から再蒸発する場合と比較するとほとんどモヤモヤと立ち昇る湯気は目立たなくなる。 The condensate discharged from the outlet 2 of the steam trap 3 is in a high temperature state, and part of the condensate evaporates again outside the narrow tube 4 while being distributed and flowing down in the narrow tube 4 formed by the gas-liquid separation membrane. The heat is dissipated into the atmosphere by being diffused into the atmosphere from a large number of pores on the surface, and the condensate is cooled. In this case, since the re-evaporated vapor that is diffused into the atmosphere is dispersed and diffused from the entire outer surface of the plurality of long tubules 4, the re-evaporated vapor stands almost completely as compared with the case where it is re-evaporated from one place. The rising steam becomes inconspicuous.
更に、復水が長尺状の細管4内を流下する間には、細管4の管壁を介して大気中への放熱もあり、エルボ5側へ流下するまでに復水は所定温度まで冷却される。
Furthermore, while the condensate flows down through the long narrow tube 4, there is heat radiation to the atmosphere through the tube wall of the narrow tube 4, and the condensate is cooled to a predetermined temperature before flowing down to the
復水が、エルボ5下端部のオリフィス・プレート7の小径貫通孔6から大気中へ排出される際にはその温度が低下しており、再度蒸発してモヤモヤと湯気が立ち昇ることはない。また、長尺状の細管4を螺旋状に曲げ加工して取り付けたことによって、細管4の放熱表面積をより多く確保することができ、復水の冷却を促進することができる。
When the condensate is discharged into the atmosphere from the small-diameter through-
なお、小径貫通孔6によってエルボ5内の流路が絞られることにより、蒸気トラップ3の出口2から排出される復水は、気液分離膜で形成した長尺状の細管4とエルボ5内に長時間滞留することとなり、大気中への放熱が一層促進される。
The condensate discharged from the outlet 2 of the steam trap 3 is narrowed in the
このように、蒸気トラップ3の出口2に気液分離膜で形成した長尺状の細管4を接続するだけで、復水の再蒸発に伴うモヤモヤとした湯気を確実に目立たなくすることのできる小型で安価な蒸気トラップの消湯気器とすることができる。 In this way, by simply connecting the long thin tube 4 formed of a gas-liquid separation membrane to the outlet 2 of the steam trap 3, the steam that has become moyah accompanying the re-evaporation of the condensate can be reliably made inconspicuous. It can be a small and inexpensive steam trap water heater.
長尺状の細管4の長さは、蒸気トラップ3から排出される復水の量、温度及び細管4の管径に応じて適宜選定することができる。 The length of the long thin tube 4 can be appropriately selected according to the amount of condensate discharged from the steam trap 3, the temperature, and the tube diameter of the thin tube 4.
1 入口
2 出口
3 蒸気トラップ
4 気液分離膜で形成した細管
5 エルボ
6 小径貫通孔
7 オリフィス・プレート
1 Inlet 2 Outlet 3 Steam trap 4 Narrow tube formed with gas-
Claims (1)
A steam / liquid separation membrane that allows vapor to permeate but does not allow liquid to permeate at the outlet side of the steam trap. The long, narrow tubules that have been formed are connected in series, and while the condensate flows down through the tubules, the condensate re-evaporates to dissipate the heat held by the condensate into the atmosphere. A steam trap water heater that makes the rising steam inconspicuous.
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JP2006134938A JP4885610B2 (en) | 2006-05-15 | 2006-05-15 | Steam trap water heater |
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JP2006134938A JP4885610B2 (en) | 2006-05-15 | 2006-05-15 | Steam trap water heater |
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JP4885610B2 JP4885610B2 (en) | 2012-02-29 |
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6199790A (en) * | 1984-10-19 | 1986-05-17 | 富士精工株式会社 | All-metal ultra-high vacuum joint |
JPS6465500A (en) * | 1987-09-04 | 1989-03-10 | Hitachi Ltd | Curved crystal type two-crystal x-ray spectroscope |
JPS6474395A (en) * | 1987-09-14 | 1989-03-20 | Tlv Co Ltd | Steam remover for steam trap |
JPH01234695A (en) * | 1988-03-14 | 1989-09-19 | Tlv Co Ltd | Discharge valve using separating membrane |
JPH11241841A (en) * | 1998-10-26 | 1999-09-07 | Japan Gore Tex Inc | Humidifying unit |
JP2007162879A (en) * | 2005-12-15 | 2007-06-28 | Tlv Co Ltd | Vapor eliminator of steam trap |
JP2007162880A (en) * | 2005-12-15 | 2007-06-28 | Tlv Co Ltd | Vapor eliminator of steam trap |
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2006
- 2006-05-15 JP JP2006134938A patent/JP4885610B2/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6199790A (en) * | 1984-10-19 | 1986-05-17 | 富士精工株式会社 | All-metal ultra-high vacuum joint |
JPS6465500A (en) * | 1987-09-04 | 1989-03-10 | Hitachi Ltd | Curved crystal type two-crystal x-ray spectroscope |
JPS6474395A (en) * | 1987-09-14 | 1989-03-20 | Tlv Co Ltd | Steam remover for steam trap |
JPH01234695A (en) * | 1988-03-14 | 1989-09-19 | Tlv Co Ltd | Discharge valve using separating membrane |
JPH11241841A (en) * | 1998-10-26 | 1999-09-07 | Japan Gore Tex Inc | Humidifying unit |
JP2007162879A (en) * | 2005-12-15 | 2007-06-28 | Tlv Co Ltd | Vapor eliminator of steam trap |
JP2007162880A (en) * | 2005-12-15 | 2007-06-28 | Tlv Co Ltd | Vapor eliminator of steam trap |
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