JPS60172787A - Steam pressure reducing valve - Google Patents
Steam pressure reducing valveInfo
- Publication number
- JPS60172787A JPS60172787A JP59026527A JP2652784A JPS60172787A JP S60172787 A JPS60172787 A JP S60172787A JP 59026527 A JP59026527 A JP 59026527A JP 2652784 A JP2652784 A JP 2652784A JP S60172787 A JPS60172787 A JP S60172787A
- Authority
- JP
- Japan
- Prior art keywords
- valve
- steam
- condensate
- pressure reducing
- reducing valve
- 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.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16K—VALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
- F16K31/00—Actuating devices; Operating means; Releasing devices
- F16K31/002—Actuating devices; Operating means; Releasing devices actuated by temperature variation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
- F22B37/26—Steam-separating arrangements
- F22B37/263—Valves with water separators
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D16/00—Control of fluid pressure
- G05D16/14—Control of fluid pressure with auxiliary non-electric power
- G05D16/16—Control of fluid pressure with auxiliary non-electric power derived from the controlled fluid
- G05D16/166—Control of fluid pressure with auxiliary non-electric power derived from the controlled fluid using pistons within the main valve
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D23/00—Control of temperature
- G05D23/01—Control of temperature without auxiliary power
- G05D23/02—Control of temperature without auxiliary power with sensing element expanding and contracting in response to changes of temperature
- G05D23/08—Control of temperature without auxiliary power with sensing element expanding and contracting in response to changes of temperature with bimetallic element
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- General Physics & Mathematics (AREA)
- Automation & Control Theory (AREA)
- Power Engineering (AREA)
- Fluid Mechanics (AREA)
- Thermal Sciences (AREA)
- Control Of Fluid Pressure (AREA)
Abstract
Description
【発明の詳細な説明】
技術分野
本発明は蒸気系に用いる減圧弁に関し、減圧弁に復水と
、塵埃・異物が入らないようにすることに係わる。DETAILED DESCRIPTION OF THE INVENTION Technical Field The present invention relates to a pressure reducing valve used in a steam system, and relates to preventing condensate, dust and foreign matter from entering the pressure reducing valve.
技術的背景
減圧弁は二次側の圧力を検出して、被制御流体の圧力エ
ネルギーを利用して作動する自刃式の調・整弁であり、
塵埃や異物が弁体と弁座の間に挾まったり、弁面を損傷
したり、受圧ピストンとシリンダの摺動部に挾まったり
すると、完全閉止ができなくなり、二次側の圧力が一次
側の圧力まで上昇する等の障害が生じる。Technical background A pressure reducing valve is a self-cutting adjustment valve that detects the pressure on the secondary side and operates using the pressure energy of the controlled fluid.
If dust or foreign matter gets caught between the valve body and valve seat, damages the valve surface, or gets caught in the sliding parts of the pressure-receiving piston and cylinder, complete closing will not be possible, and the pressure on the secondary side will be lower than that on the primary side. Problems such as rising pressure may occur.
また、蒸気は冷却されると復水になり、特に、通気初期
は配管系が低鍋であるので多量の復水が発生し、蒸気用
減圧弁には多かれ少なかれ蒸気と共に復水が流入する。In addition, when steam is cooled, it becomes condensate, and in particular, at the beginning of ventilation, a large amount of condensate is generated because the piping system is a low pot, and more or less condensate flows into the steam pressure reducing valve together with the steam.
この復水のために、減圧弁はハンチング・ヂャタリング
等で振動が発生し、作動に支障をぎたすばかりでなく、
配管系にウォータハンマを誘発して連結した機器を損傷
したり、また復水に接する部分が腐食しやすくなり、寿
命を縮める原因となる。Due to this condensation, vibrations occur in the pressure reducing valve due to hunting and jitter, which not only hinders operation but also
Water hammer can occur in the piping system, damaging connected equipment, and parts that come into contact with condensate are more likely to corrode, shortening the service life.
従って、蒸気用減圧弁では、塵埃・異物ばかりでなく、
復水の流入も防がなければならない。Therefore, steam pressure reducing valves are not only susceptible to dust and foreign matter.
Inflow of condensate must also be prevented.
従来技ｊりｉとその問題点
そこで、従来は、減圧弁の上流側の一次側の配管にスト
レーナを配置し、さらにその上流側の配管には立ち下が
り配管を分岐させて、その分岐配管にストレ〜すとスチ
ームトラップを配置していた。従って、先ず復水がスチ
ームトラップで系外に排除され、次に蒸気に混入する塵
埃・異物がストレーナで濾過され、その結束、復水も塵
埃・異物も含まない蒸気だけが減圧弁に導入されること
になる。Conventional techniques and their problems Therefore, in the past, a strainer was placed in the primary piping on the upstream side of the pressure reducing valve, and a falling piping was branched to the piping on the upstream side, and a strainer was placed in the piping on the upstream side. A steam trap was placed. Therefore, first, condensate is removed from the system by a steam trap, then dust and foreign matter mixed in with the steam are filtered out by a strainer, and only the steam that does not contain condensate, dust, or foreign matter is introduced into the pressure reducing valve. That will happen.
しかし、この場合でも、完全閉止ができず、漏れが生じ
て二次側の圧力が上昇することがある。However, even in this case, complete closure may not be possible, causing leakage and increasing pressure on the secondary side.
これはストレーナを通過する微細な塵埃・放物によるも
のである。ストレーナのスクリーンのこし孔、あいろは
メツシュの大きさを小さくずればＪ：いが、これも圧力
損失や目詰りの観点から、実際上限界がある。This is due to fine dust and parabolites passing through the strainer. It would be possible to reduce the size of the strainer screen's strainer holes and the mesh size, but this also has a practical limit in terms of pressure loss and clogging.
技術的課題
本発明の技術的課題は、ストレーナを通過した微細な塵
埃・異物を減圧弁に至るまでに系外に排除してしまうこ
とである。Technical Problem The technical problem of the present invention is to eliminate fine dust and foreign matter that have passed through the strainer out of the system before reaching the pressure reducing valve.
技術的手段
上記の技術的課題を解決するために講じた本発明の技術
的手段は、
（イ） ストレーナと減圧弁の弁口の間に旋回流を起こ
して塵埃・異物を復水と共に蒸気から分離する手段を設
（プ、
（ロ） 復水や塵埃・異物を系外に排除する弁を設けた
、
ものである。Technical Means The technical means of the present invention taken to solve the above technical problems are as follows: (a) A swirling flow is generated between the strainer and the valve opening of the pressure reducing valve to remove dust and foreign matter from the steam together with condensate. (b) A valve is installed to remove condensate, dust, and foreign matter from the system.
ここで、旋回流は流体通路の内壁や、羽根や、孔の方向
によって流体を所定の方向に向かわせることによって起
こすことができる。例えば、弁口の周りに環状の通路を
形成し、そこに羽根を配置したり、孔を設けたりする。Here, the swirling flow can be generated by directing the fluid in a predetermined direction by the inner wall of the fluid passage, the vane, or the direction of the hole. For example, an annular passage may be formed around the valve opening, in which vanes may be placed or holes may be provided.
また、ストレーナは、例えば、円筒形状のスクリーンを
上記の環状通路を囲んで配置する。Further, the strainer includes, for example, a cylindrical screen arranged surrounding the annular passage.
復水排除弁は適当な時期に手動で開閉する弁でも、常時
一定量流出するオリフィスでもよいが、好ましくは、ス
チームトラップ、それも弁室内に圧力変動を引き起こさ
ないフロート式スチームトラップが適している。The condensate removal valve may be a valve that is manually opened and closed at appropriate times, or an orifice that always releases a constant amount of water, but preferably a steam trap, especially a float type steam trap that does not cause pressure fluctuations in the valve chamber. .
技術的手段の作用 上記の技術的手段の作用は下記の通りである。Action of technical means The operation of the above technical means is as follows.
蒸気は先ずストレーナに入り、スクリーンのこし孔にり
も大きい塵埃・異物はそこでスクリーンに補足される。Steam first enters the strainer, where the screen captures dust and foreign matter that are too large to fit through the strainer holes in the screen.
スクリーンを通過した蒸気及び復水とｉ故細な塵埃・異
物は所定の方向に流れを向かわせる羽根や孔の作用で旋
回し、遠心力の作用で復水ど塵埃・異物は外側を周り、
周囲の壁を伝わって落下し、排除弁で系外に排除される
。蒸気は旋回流の中央部にあって弁口に向かう。Steam and condensate that have passed through the screen, as well as fine dust and foreign matter, are rotated by the action of vanes and holes that direct the flow in a predetermined direction, and the condensate, dust, and foreign matter are rotated around the outside by the action of centrifugal force.
It falls along the surrounding walls and is removed from the system by the exclusion valve. The steam is in the center of the swirling flow and heads toward the valve port.
特有の効果
ストレーナのスクリーンを通過する微細な塵埃・異物の
多くが減圧弁の弁口に至るまでに、蒸気から分離されて
系外に排除されるので、弁部や摺動部での挾み込み、弁
部の摩耗・損傷が少なくなり、不完全閉止が少なくなる
。Unique Effect: Most of the fine dust and foreign matter that pass through the strainer screen are separated from the steam and removed from the system by the time they reach the valve opening of the pressure reducing valve. This reduces wear and damage to the valve part and reduces incomplete closure.
フルート式スチームトラップ等の復水排除弁はストレー
ナの下流に位置するので、ストレーナを減圧弁と排除弁
とに兼用できる。Since a condensate removal valve such as a fluted steam trap is located downstream of the strainer, the strainer can be used both as a pressure reducing valve and as a removal valve.
旋回流を起こして復水と微細な塵埃・異物を分離するの
で、分離効率が極めて良くなる。Separation efficiency is extremely high because it creates a swirling flow to separate condensate from fine dust and foreign matter.
実施例の説明
上記の技術的手段の具体例を示す実施例（図面参照）を
説明する。DESCRIPTION OF EMBODIMENTS An embodiment (see drawings) showing a specific example of the above technical means will be described.
減圧弁１の主要部分は従来周知のものとほぼ同じなので
簡単に説明する。本体２４に入口１３と出口１４が形成
され、両者は弁口８を通して連通している。弁口８を開
閉する主弁７は弁棒で受圧ピストン５に連結している。The main parts of the pressure reducing valve 1 are almost the same as those conventionally known, so they will be briefly explained. An inlet 13 and an outlet 14 are formed in the main body 24 and communicate with each other through the valve port 8. A main valve 7 that opens and closes a valve port 8 is connected to a pressure receiving piston 5 through a valve stem.
ピストン５の背圧はパイロット弁２で制御される。入口
側の圧力は通路６でパイロット弁２に導かれる。パイロ
ット弁２はスプリング４で弾性的に付勢されたダイヤフ
ラム３で操作される。ダイヤフラム３の下面には通路２
５を通して出口側の圧力が作用する。The back pressure of the piston 5 is controlled by a pilot valve 2. The pressure on the inlet side is led to the pilot valve 2 through a passage 6. The pilot valve 2 is operated by a diaphragm 3 elastically biased by a spring 4. Passage 2 is on the bottom surface of diaphragm 3.
The pressure on the outlet side acts through 5.
弁口８を囲んで円筒形状の隔壁９を設け、さらにその隔
壁９に円筒形状の障壁１６を延長的に螺着し、環状通路
１１を形成する。環状通路１１の外側は円筒形状のスク
リーン１０で囲む。スクリーン１ｏの外周には入口１３
に連通した環状空間２６を形成する。A cylindrical partition 9 is provided surrounding the valve port 8, and a cylindrical barrier 16 is extended and screwed onto the partition 9 to form an annular passage 11. The outside of the annular passage 11 is surrounded by a cylindrical screen 10. There is an entrance 13 on the outer periphery of the screen 1o.
An annular space 26 is formed which communicates with the .
環状通路１１の下部には旋回羽根１２と末広がりの水切
り部材１５を、隔壁９と障壁１６の間に挾んで配置する
。旋回羽根１２は環状通路１１の全周に突出し、各羽根
が同一方向に斜に曲げである。At the bottom of the annular passage 11, a swirling vane 12 and a draining member 15 that widens toward the end are placed between the partition wall 9 and the barrier 16. The swirling vanes 12 protrude around the entire circumference of the annular passage 11, and each vane is obliquely bent in the same direction.
本体２４にトラップ本体２７をボルト２３で取り付け、
トラップ本体２７に下蓋２８をボルト２９で取り付ける
。内部の弁室１９には球形の中空フロート２０を自由状
態で収容する。下蓋２８には弁座２１を取り付ける。参
照番号２２は排水口である。Attach the trap body 27 to the body 24 with bolts 23,
A lower cover 28 is attached to the trap body 27 with bolts 29. The internal valve chamber 19 accommodates a spherical hollow float 20 in a free state. A valve seat 21 is attached to the lower cover 28. Reference number 22 is a drain port.
障壁１６を形成する部材は中心部に主弁７の弁棒を案内
する部材３０を有し、両者は横断壁で一体に形成してあ
り、横断壁には通気孔１７が開けである。案内部材３０
の下端にフロートの天蓋１８を取り付ける。天ｌ１１８
は上に凸の球面の皿形状で、その外周縁はし・ラップ本
体２７の内周壁から離れており、その間に微少な空間が
形成される。The member forming the barrier 16 has a member 30 in its center that guides the valve stem of the main valve 7, and both are integrally formed with a transverse wall, and a ventilation hole 17 is opened in the transverse wall. Guide member 30
Attach the float canopy 18 to the lower end of the float. Ten l118
has an upwardly convex spherical dish shape, and its outer peripheral edge is separated from the inner peripheral wall of the edge/wrap body 27, with a small space formed therebetween.
天蓋１８の中央寄りの部位に通気孔を開けてもよい。A ventilation hole may be provided in a portion closer to the center of the canopy 18.
蒸気は入口１３から環状空間２６に入り、スクリーン１
０を通過して環状通路−１１に入る。環状通路１１の蒸
気の一部は通路６を通してパイロット弁２に供給される
。他の大部分の蒸気は、弁口８が開くと、旋回羽根１２
の作用で一定方向に曲げられて旋回し、遠心力の作用で
、復水と微細な塵埃・異物は外側を回って外周壁に沿っ
てトラップの弁ｖ１つに落下する。内側の蒸気は障壁１
６の下端を回ってその内部に入り、通気孔１７から弁口
８を通り出口１４に向かう。Steam enters the annular space 26 through the inlet 13 and enters the screen 1
0 and enters the annular passage-11. A portion of the steam in the annular passage 11 is supplied to the pilot valve 2 through the passage 6. When the valve port 8 is opened, most of the other steam is transferred to the swirl vane 12.
The trap is bent and rotated in a certain direction by the action of the trap, and by the action of the centrifugal force, the condensate, fine dust, and foreign matter go around the outside and fall along the outer circumferential wall into one valve v of the trap. Steam inside is barrier 1
6 and enters its interior, passing through the vent hole 17 and the valve port 8 to the outlet 14.
旋回羽根１２に付着する復水は水切り部材１５の作用で
旋回の外側に振り出される。復水は天蓋１８の外周の空
き間を通して弁室に入り、蒸気で四゛き上げられて減圧
弁の弁口８に運ばれることがない。同時に、旋回流れの
影響は天蓋１８で遮られフロート２０に及ばない。The condensate adhering to the swirl vane 12 is blown out to the outside of the swirl by the action of the draining member 15. The condensate enters the valve chamber through the space on the outer periphery of the canopy 18, is lifted up by steam, and is not carried to the valve port 8 of the pressure reducing valve. At the same time, the influence of the swirling flow is blocked by the canopy 18 and does not reach the float 20.
フロー１〜２０は弁室１９の復水に浮いて上下動し、弁
座２１に離着塵して、蒸気を逃がさずに復水を自動的に
排出する。Flows 1 to 20 float on the condensate in the valve chamber 19 and move up and down, deposit dust on the valve seat 21, and automatically discharge the condensate without letting steam escape.
この実施例のように、弁口の周りに環状通路を設けてそ
こで旋回を起こすようにし、その環状通路を囲んで円筒
形状のスクリーンを配置する４１！、 ３１にすれば、
コンパクトな構造になり、小形になると共に、蒸気がス
クリーンの全周囲から流入するようになるので、スクリ
ーンの目詰まり速度が遅くなり、塵埃・異物のブロー間
隔を長（できる。As in this embodiment, an annular passage is provided around the valve port to cause swirling therein, and a cylindrical screen is placed surrounding the annular passage 41! , If you set it to 31,
It has a compact structure and is small, and since steam flows in from all around the screen, the speed at which the screen gets clogged is slowed down, and the interval between blowing dust and foreign matter can be extended.
また、復水排除弁にフロート式スチームトラップを用い
れば、復水を自動的に排除するだけでなく、弁室内の圧
力を変動させずに開閉弁するので、減圧奔の作動に影響
を及ぼさない。Additionally, if a float-type steam trap is used as the condensate removal valve, not only will it automatically remove condensate, but it will also open and close the valve without changing the pressure inside the valve chamber, so it will not affect the operation of the pressure reducing force. .
図は本発明の実施例の蒸気用減圧弁の断面図である。
７：主弁
８：弁口 １０：環状通路
１２：旋回羽根 １３：入口
１４：出口
２０ニスチームトラツプのフロート
２１：弁座 ２６：環状空間
手続祁１正書（白化）
２１発明の名称
蒸気用減圧弁
３、補正をする者
事件との関係 特許出願人
住所 東京都千代田区内幸町２丁目２番３号日比谷国際
ビル８階８１０区
４、補正の対象
〈１）明細書の発明の詳細な説明の欄
（２）明ｉ書の図面の簡単な説明の欄
（３）図面
５、補正の内容
（１）明ｍ但第６頁第１５行の「図面」を、「第１図］
と訂正する。
（２）明細書第１０頁第８行から第１６行までを下記の
通りに訂正する。
記
他の実施例の説明
次に、他の実施例（第２図参照）を説明する。
第２図の減圧弁は大部分が第１図のものと同じなので、
その上部の図示を省略し、また第１図に対応する部分に
は第１図と同じ参照番号を付して説明を省略する。
パイロット弁２に入口側の蒸気を導く通路６を、円筒形
状の隔壁９の内側に開口させ、旋回羽根１２で復水や塵
埃・異物を分離した乾いた清浄゛な蒸気がパイロット弁
２にも確実に供給されるようにした。
また、本体２４の下端には、排水口５１を形成した下蓋
５０を取り付け、スチームトラップ５２は排水通路５３
に外付けするようにした。
４、図面の簡単な説明
第１図は本発明の実施例の蒸気用減圧弁の断面図、第２
図は他の実施例の蒸気用減圧弁の一部を省略した断面図
である。
７：主弁
８：弁口 １０：環状通路
１２：旋回羽根 １３二人ロ
１４：出口
２０ニスチームトラツプのフロート
２１：弁座 ２６：環状空間
５０：下蓋 ５１：排水口
５２；スチームトラップ
図日寸ノ目ｌ！Ｉ１ｇ＝′３−シｎ’ｈリーーＹ−′
（３）願書に添付した図面の断面図の図番を第１図とす
る。
（４）添付の図面の断面図を第２図をとして追加する。
６、添付書類の目録
（１）図面（鯖２図） １通
（２） ｌ＠４： （簿１図）ｔ ｔｃ入し旧ｎ面の写
し １４特開昭ＧＯ−１７２７８７（５）
第 １１４The figure is a sectional view of a steam pressure reducing valve according to an embodiment of the present invention. 7: Main valve 8: Valve port 10: Annular passage 12: Swirling vane 13: Inlet 14: Outlet 20 Nisteam trap float 21: Valve seat 26: Annular space procedure Qi 1 official text (whitewashing) 21 Name of invention Steam Pressure reducing valve for use 3, Relationship with the case of the person making the amendment Patent applicant address: 4, 810, 8th floor, Hibiya Kokusai Building, 2-2-3 Uchisaiwai-cho, Chiyoda-ku, Tokyo Subject of amendment <1) Detailed description of the invention in the specification Explanation column (2) Brief explanation column for the drawings in the document (3) Drawing 5, contents of amendment (1) Note that "Drawing" on page 6, line 15 has been changed to "Fig. 1"
I am corrected. (2) Lines 8 to 16 of page 10 of the specification are corrected as follows. Description of Other Embodiments Next, another embodiment (see FIG. 2) will be described. Most of the pressure reducing valves in Figure 2 are the same as those in Figure 1, so
Illustration of the upper part is omitted, and parts corresponding to those in FIG. 1 are given the same reference numerals as in FIG. 1, and explanations thereof are omitted. A passage 6 that guides steam on the inlet side to the pilot valve 2 is opened inside the cylindrical partition wall 9, and dry, clean steam with condensate, dust, and foreign matter separated by the swirl vanes 12 is also supplied to the pilot valve 2. Ensured supply. Further, a lower lid 50 having a drain port 51 is attached to the lower end of the main body 24, and a steam trap 52 is connected to a drain passage 53.
I installed it externally. 4. Brief explanation of the drawings Fig. 1 is a sectional view of a steam pressure reducing valve according to an embodiment of the present invention, Fig. 2 is a sectional view of a steam pressure reducing valve according to an embodiment of the present invention.
The figure is a partially omitted cross-sectional view of a steam pressure reducing valve according to another embodiment. 7: Main valve 8: Valve port 10: Annular passage 12: Swirling vane 13 Two-person rotor 14: Outlet 20 Nisteam trap float 21: Valve seat 26: Annular space 50: Lower cover 51: Drain port 52; Steam trap Figure day size l! I1g='3-Shin'h Lee-Y-' (3) The figure number of the sectional view of the drawing attached to the application is FIG. 1. (4) Add a cross-sectional view of the attached drawings as Figure 2. 6. List of attached documents (1) Drawings (Mackerel 2 drawings) 1 copy (2) l@4: (Book 1 drawing) t tc copy of old n side 14 JP-A-172787 (5) No. 114
Claims (4)
レーナと減圧弁の弁口との間に旋回流を起こして塵埃・
異物を復水と共に蒸気から分離する手段を設け、分離さ
れた復水や塵埃・異物を系外に排除する弁を設けた蒸気
用減圧弁。(1) A strainer is installed on the inlet side of the pressure reducing valve, and a swirling flow is created between the strainer and the valve opening of the pressure reducing valve to remove dust and dirt.
A pressure reducing valve for steam that is equipped with a means to separate foreign matter from steam together with condensate, and a valve that removes the separated condensate, dust, and foreign matter from the system.
の環状通路に旋回分離手段を配置した、特許請求の範囲
第１項記載の蒸気用減圧弁。(2) The pressure reducing valve for steam according to claim 1, wherein an annular passage is formed surrounding the valve opening of the pressure reducing valve, and a swirl separation means is disposed in the annular passage.
した、特許請求の範囲第２項記載の蒸気用減圧弁。(3) The steam pressure reducing valve according to claim 2, wherein a cylindrical screen is arranged surrounding the annular passage.
プを用いた、特許請求の範囲第１項記載の蒸気用減圧弁
。(4) 1. The steam pressure reducing valve according to claim 1, which uses a float steam trap as the condensate removal valve.
Priority Applications (26)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59026527A JPH0658607B2 (en) | 1984-02-15 | 1984-02-15 | Pressure reducing valve for steam |
| NZ209289A NZ209289A (en) | 1983-10-27 | 1984-08-20 | Gas pressure reducing valve with liquid separator |
| AU32266/84A AU569538B2 (en) | 1983-10-27 | 1984-08-22 | Reducing valve equipped with a vapor-liquid separator |
| KR1019840005397A KR850003775A (en) | 1983-10-27 | 1984-09-03 | Pressure reducing valve with separator |
| IN611/CAL/84A IN163096B (en) | 1983-10-27 | 1984-09-03 | |
| CA000464088A CA1243919A (en) | 1983-10-27 | 1984-09-26 | Reducing valve equipped with a vapour-liquid separator |
| NL8403039A NL189151C (en) | 1983-10-27 | 1984-10-05 | GAS REDUCING VALVE AND LIQUID SEPARATOR. |
| LU85592A LU85592A1 (en) | 1983-10-27 | 1984-10-15 | REDUCING VALVE, PROVIDED WITH A VAPOR LIQUID SEPARATOR |
| FI844093A FI76634C (en) | 1983-10-27 | 1984-10-17 | REDUCERINGSVENTIL FOERSEDD MED EN AONGA-VAETSKA-SEPARATOR. |
| CH5025/84A CH669647A5 (en) | 1983-10-27 | 1984-10-18 | |
| DE19843438115 DE3438115A1 (en) | 1983-10-27 | 1984-10-18 | REDUCING VALVE, PROVIDED WITH A STEAM LIQUID SEPARATOR |
| GB08426671A GB2149147B (en) | 1983-10-27 | 1984-10-22 | A reducing valve equipped with a vapor-liquid separator |
| BR8405363A BR8405363A (en) | 1983-10-27 | 1984-10-23 | REDUCING VALVE |
| GR80745A GR80745B (en) | 1983-10-27 | 1984-10-23 | Reducing valve equipped with vapor-liquid separator |
| PT79402A PT79402B (en) | 1983-10-27 | 1984-10-24 | A reducing valve equipped with a vapor-liquid separator |
| NO844232A NO158828C (en) | 1983-10-27 | 1984-10-24 | REDUCTION VALVE EQUIPPED WITH STEAM / WASHER Separator. |
| BE2/60526A BE900895A (en) | 1983-10-27 | 1984-10-25 | REDUCING VALVE FITTED WITH A VAPOR FLUID SEPARATOR. |
| AT3400/84A AT392341B (en) | 1983-10-27 | 1984-10-25 | PRESSURE REDUCER VALVE WITH A LIQUID SEPARATOR |
| ES84537049A ES537049A0 (en) | 1983-10-27 | 1984-10-25 | IMPROVEMENTS IN REDUCING VALVES |
| IT2331884A IT1196311B (en) | 1983-10-27 | 1984-10-25 | REDUCTION VALVE EQUIPPED WITH A STEAM-LIQUID SEPARATOR |
| SE8405343A SE459984B (en) | 1983-10-27 | 1984-10-25 | REDUCTION VALVE WITH ANTI-WATER SPARE PARTS |
| MX84203167A MX160557A (en) | 1983-10-27 | 1984-10-25 | IMPROVEMENTS IN REDUCING VALVE EQUIPPED WITH A LIQUID VAPOR SEPARATOR |
| FR8416454A FR2554211B1 (en) | 1983-10-27 | 1984-10-26 | REDUCTION VALVE EQUIPPED WITH A STEAM-LIQUID SEPARATOR |
| DK510784A DK162949C (en) | 1983-10-27 | 1984-10-26 | REDUCING VALVE |
| KR2019870022607U KR880004076Y1 (en) | 1983-10-27 | 1987-12-21 | A reducing valve equipped with a vapor-liquid separator |
| US07/319,417 US4860782A (en) | 1983-10-27 | 1989-03-03 | Reducing valve equipped with a vapor-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59026527A JPH0658607B2 (en) | 1984-02-15 | 1984-02-15 | Pressure reducing valve for steam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60172787A true JPS60172787A (en) | 1985-09-06 |
| JPH0658607B2 JPH0658607B2 (en) | 1994-08-03 |
Family
ID=12195948
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59026527A Expired - Fee Related JPH0658607B2 (en) | 1983-10-27 | 1984-02-15 | Pressure reducing valve for steam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0658607B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100954720B1 (en) | 2009-11-09 | 2010-04-23 | 주식회사 신흥밸브 | Pressure reducing valve |
| CN112197161A (en) * | 2020-10-10 | 2021-01-08 | 济南高瓴机械科技有限公司 | Multifunctional steam trap |
-
1984
- 1984-02-15 JP JP59026527A patent/JPH0658607B2/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100954720B1 (en) | 2009-11-09 | 2010-04-23 | 주식회사 신흥밸브 | Pressure reducing valve |
| CN112197161A (en) * | 2020-10-10 | 2021-01-08 | 济南高瓴机械科技有限公司 | Multifunctional steam trap |
| CN112197161B (en) * | 2020-10-10 | 2021-07-27 | 立信阀门集团有限公司 | Multifunctional steam trap |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0658607B2 (en) | 1994-08-03 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |