CN1003803B - 冷凝物的分离和排出装置 - Google Patents
冷凝物的分离和排出装置 Download PDFInfo
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
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- 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
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- 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
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- F16T1/00—Steam traps or like apparatus for draining-off liquids from enclosures predominantly containing gases or vapours, e.g. gas lines, steam lines, containers
- F16T1/20—Steam traps or like apparatus for draining-off liquids from enclosures predominantly containing gases or vapours, e.g. gas lines, steam lines, containers with valves controlled by floats
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F16T—STEAM TRAPS OR LIKE APPARATUS FOR DRAINING-OFF LIQUIDS FROM ENCLOSURES PREDOMINANTLY CONTAINING GASES OR VAPOURS
- F16T1/00—Steam traps or like apparatus for draining-off liquids from enclosures predominantly containing gases or vapours, e.g. gas lines, steam lines, containers
- F16T1/20—Steam traps or like apparatus for draining-off liquids from enclosures predominantly containing gases or vapours, e.g. gas lines, steam lines, containers with valves controlled by floats
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Abstract
一种冷凝物的分离和排出装置包括:输入口,安装在上述壳体内的筒形构件,该构件与上述壳体内壁表面以分隔开的方式安装在上述壳体内,由上述壳体内壁表面和上述筒形构件所构成的分离器,和安装在上述壳体内的上述筒形构件下的汽阱部分,该汽阱部分包括一个具有浮子的冷凝物排出阀和一个罩在它上面的浮子盖,其改进特征在于使上述筒形构件的下端与上述浮子盖顶部之间的距离A和上述汽阱部分的壳体内径B二者关系是A/B不小于0.4的关系。
Description
本发明涉及包括汽阱被整体地耦合到分离器上的冷凝物分离和排出的装置,例如使用在一般的蒸汽管道中的分离器,特别涉及具有改进的排泄分离效率的冷凝物的分离和排出装置。
通常,常见的是,独立构成的汽阱,分离器的减压阀等是一个连接到另一个上,并被装配在蒸汽管道中的。
在已有技术中,要完成,在蒸汽管道中安装象减压阀、分离器和汽阱等组合装置的管道作业是非常困难的,同样调节这些组合装置中的每一个设备也是困难的。为了克服这个缺陷,就考虑到把这些组合装置整体地相互耦合。
在这样的整体结构的冷凝物的分离和排出装置中,筒形构件安装在一壳体中,在该壳体的内壁表面和筒形构件外表面之间形成一蒸汽引入通道作为分离器,使从输入口引入的蒸汽沿着壳体的内壁表面向下旋流,使通过筒形构件输送的蒸汽从输出口输出。另外,包括一个排出阀在内的汽阱部分被安装在筒形构件的下面,上述排出阀具有一个浮子和盖在浮子上的浮子盖。
一般情况下,蒸汽管的蒸汽以最大近似于40米/秒高速流动,由此,通过蒸汽引入通道被引到汽阱的蒸汽是高速猛烈旋流的。因此,如果作为蒸汽从输入口导向输出口的筒形构件的下端和浮子盖的顶部之间距离是短的话,由旋流的蒸汽象旋风一样把沉积到浮子盖上的水滴和聚集在汽阱部分底部的冷凝物向上回旋,并通过输出口向外输送。显然大大地增加筒形构件的下端到浮子盖顶部之间的距离可以解决这个问题。但是会不利地使得冷凝物的分离和排出装置的尺寸变大。
本发明的目的是在不使装置的尺寸变成不必要大的前提下,在既具有分离器作用,又具有汽阱作用的冷凝物的分离和排出装置中尽可能地改进从蒸汽中分离冷凝物的效率。
根据本发明,在具有分离器部分和汽阱部分的冷凝物的分离和排出装置中,其改进的特征在于筒形构件的下端到浮子盖顶部之间距离为A和汽阱部分的壳体内径为B,两者关系是A/B不小于0.4,这样可提高冷凝物的分离效率。该装置也适用于从压缩空气或任何其它气体及蒸汽中分离和排出排泄物。
根据本发明,从输入口引入的含冷凝物的气体在引入通道中旋流而下,并被输送到汽阱部分。在此同时,冷凝物从蒸汽中分离出来。然后冷凝物基本上沿着汽阱部分和壳体内壁表面落下,并聚集在汽阱部分的底部。另一方面,气体通过筒形构件上升,并从输出口输出。当在汽阱部分的底部聚集冷凝物达到预定的水平时,浮子被提升从而打开了排出阀,并排出冷凝物。
在本发明的冷凝物的分离和排出装置中,筒形构件的下端到浮子盖顶部之间距离为A和汽阱部分的内径为B,两者关系是A/B不小于0.4,也就是,距离A不小于内径B的40%。因此沉积到浮子盖顶部的水滴和聚集在汽阱部分底部的冷凝物不被气体旋流向上,而让该气体通过筒形构件,并从输出口向外输送。
附图是本发明最佳实施例中减压阀的垂直剖视图。
1…减压阀部分2…汽阱部分4…初始蒸汽压力的蒸汽输入口5…二次蒸汽压力的蒸汽输出口7…主阀21…筒形构件26…汽阱座27…浮子28…小孔29…浮子盖34…蒸汽引入通道(分离器部分)
本发明的最佳实施例陈述如下:在该最佳实施例中,冷凝物的分离和排出装置包括一个减压阀。参考所示的本最佳实施例的垂直剖面图、编号1和2分别标明减压阀部分和耦合到减压阀下端的汽阱部分。减压阀部分1包括:在壳体3一侧引入具有初始压力的蒸汽的输入口4和在输入口4相反的一侧输送二次减压的蒸汽的输出口5。主阀座6装在壳体3中,主阀7由螺旋弹簧8对着主阀座6加力。活塞9的活塞杆10是紧靠在主阀7的上端。编号11标明为二次蒸汽压力的调节螺钉。当该调节螺钉11被拧紧时,隔膜14被螺旋弹簧12和装在螺旋弹簧12下端的推杆构件13压下。其结果导杆15对着螺旋弹簧17的偏置力被压下,从而打开了导阀16。装备第一通道18为把初始压力蒸汽引入导阀16的下部空间。装备第二通道19为了把通过导阀16的初始压力蒸汽引入活塞9的上部空间。装备第三通道为了把从输出口5来的二次压力蒸汽引导入隔膜14的下部空间。根据需要还装备滤器32和滤网33。
在下面稍微扩开成喇叭状的筒形构件21是被装配到位于壳体3中部的主阀座的一部分上。该筒形构件21借助导向和支撑构件22,在该构件21的外周若干个位置上,例如四个位置上将其固定到壳体3内。作为分离器的蒸汽引入通道34是在筒形构件21和壳体3内周之间形成的。流过蒸汽引入通道34的蒸汽是旋流的。支撑主阀7的阀杆23的筒体24是被安装在筒形构件21内,并且例如通过四个支撑架25被装配在筒形构件的内壁上。
包括汽阱座26和浮子27的冷凝物排出阀被安装在汽阱部分2的底部。浮子27罩有象圆帽形的浮子盖29,在浮子盖29的上部具有小型排气孔28。浮子盖29通过如图中两处虚线所示的法兰30和螺钉31被安装在汽阱部分2的底部。
根据本发明,筒形构件21的下端和浮子盖29的顶端之间的距离A与汽阱部分2的内径B成一定关系,以致A/B不小于0.4,而与输入口4的口径C无关,从而冷凝物的分离效率是可以改进的。下表给出了在冷凝物的分离和排出装置中对各种口径C提供95%或95%以上的高冷凝物分离效率的每个A、B和A/B值。
表
口径C 距离A 内直径B A/B
(mm) (mm) (mm)
15 37.2 70 0.531
20 37.2 70 0.531
25 40.9 79.4 0.515
32 48.8 103.3 0.472
40 48.8 103.3 0.472
50 57.9 131.4 0.441
在上述的实施例中,首先通过二次蒸汽压力调节螺钉11来调节一个预定的二次蒸汽压力。从输入口4引入的一部分高压蒸汽(初始蒸汽压力)通过第一通道18进入导阀16下面的空间。然后,该蒸汽从以螺钉11调定的具有预定开度的导阀16流过第二通道19进入活塞9的上部空间。结果,活塞9顶着螺旋弹簧8的偏置力下降以便打开主阀7。从输入口4引入的大部分蒸汽允许流过。壳体3的内壁和筒形构件21的外周表面之间所构成的蒸汽引入通道34,而且猛烈地向下旋流到汽阱部分2。冷凝物是沿着汽阱部分2的内壁落下或与浮子盖29碰撞而落到汽阱部分2的底部,而仅仅允许蒸汽在筒形构件21内通过主阀7上升,并且作为二次压力的蒸汽从输出口5输送。一部分二次压力蒸汽通过第三通道20进入隔膜14的下部空间。当二次蒸汽压力增加时,隔膜14顶着螺旋弹簧12的偏置力被压向上,以便减少导阀16的开度,也就是减少了主阀7的开度,从而减少二次蒸汽压力。相反,当二次蒸汽压力下降到等于或大于调定值时,通过与以上相反的操作增加主阀7的开度,以便使二次蒸汽压力返回到调定值。
因此,把与冷凝物分离的蒸汽压力降低到预定的二次蒸汽压力,然后从输出口5输送出这与冷凝物分离的蒸汽。
虽然上述的实施例揭示了包括减压阀在内的冷凝物的分离和排出装置,但是甚至当在冷凝物的分离和排出装置中不包括减压阀时,冷凝物的分离效率是几乎不变的。
根据本发明,由于冷凝物的分离和排出装置具有从气体中分离冷凝物的分离器作用以及排出被分离的冷凝物的汽阱作用,蒸汽管道作业可以被大大简化。另外,由于减压阀可以装配在冷凝物的分离和排出装置中,所以在安装减压阀的情况下其装置更加有效。再则,在不增加汽阱部分尺寸的情况下,设法调定浮子盖顶部与筒形构件下端之间距离A和汽阱部分的内径B之间的大小关系,以便提供一个高冷凝物分离效率。据此,与单独的分离器和汽阱被相互连接的常用情况相比较,本冷凝物的分离和排出装置可以更加大大地压缩体积。甚至当在装置中包括减压阀时,该装置的总尺寸与常用的分离式减压阀相比较也没有增大多少,而在分离器部分可以获得95%或大于95%的高冷凝物分离效率。
Claims (1)
1、一种冷凝物的分离和排出装置包括:一个输入口,一个壳体,一个安装在上述壳体中的筒形构件,一个由上述壳体内壁表面和上述筒形构件所构成的分离器,一个输送流过上述筒形构件的气体到上述壳体的外面的输出口,和一个装在上述壳体内的筒形构件下面的汽阱部分,该汽阱部分包括一个冷凝物排出阀,其冷凝物排出阀具有一个浮子和盖在浮子上的浮子盖,其特征在于上述筒形构件的下端到上述浮子盖顶部之间距离为A和上述汽阱部分的壳体内径为B两者关系是A/B不小于0.4。
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60205629A JPS6267397A (ja) | 1985-09-17 | 1985-09-17 | 復水分離排出器 |
JP205629/85 | 1985-09-17 |
Publications (2)
Publication Number | Publication Date |
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CN86105071A CN86105071A (zh) | 1987-03-18 |
CN1003803B true CN1003803B (zh) | 1989-04-05 |
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CN86105071.1A Expired CN1003803B (zh) | 1985-09-17 | 1986-08-16 | 冷凝物的分离和排出装置 |
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Country | Link |
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US (1) | US4867767A (zh) |
JP (1) | JPS6267397A (zh) |
KR (1) | KR920008197B1 (zh) |
CN (1) | CN1003803B (zh) |
BE (1) | BE905442A (zh) |
CA (1) | CA1273262A (zh) |
CH (1) | CH671086A5 (zh) |
DE (1) | DE8624703U1 (zh) |
ES (1) | ES2002513A6 (zh) |
FR (1) | FR2587443B1 (zh) |
GB (1) | GB2189878B (zh) |
GR (1) | GR862338B (zh) |
IT (1) | IT1197232B (zh) |
NZ (1) | NZ217606A (zh) |
PH (1) | PH24329A (zh) |
PT (1) | PT83391B (zh) |
ZA (1) | ZA866051B (zh) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3806756C2 (de) * | 1988-03-02 | 1996-12-05 | Armaturen Und Autogengeraetefa | Druckluftfilter |
ES2073087T3 (es) * | 1990-10-15 | 1995-08-01 | Tlv Co Ltd | Purgador de vapor automatico de flotador libre. |
FR2691382B1 (fr) * | 1992-05-22 | 1994-09-09 | Cit Alcatel | Installation de pompage pour pomper une enceinte contenant des gaz mélangés à des particules solides ou susceptibles de générer des particules ou condensats solides. |
US5476525A (en) * | 1994-03-01 | 1995-12-19 | Bekedam; Martin | Steam condensate recovery component |
AUPN865596A0 (en) * | 1996-03-13 | 1996-04-04 | Bellomo, Erasmo Mimmo | Air drying and purification system |
GB2440548B (en) * | 2006-08-02 | 2011-07-06 | Spirax Sarco Ltd | Condensate Traps |
HUE041943T2 (hu) * | 2007-03-06 | 2019-06-28 | Tlv Co Ltd | Úszós szelepkészülék, valamint eljárás úszós szelepkészülék tisztítására |
JP5267163B2 (ja) * | 2008-12-04 | 2013-08-21 | 三浦工業株式会社 | 気固液分離器 |
WO2017175744A1 (ja) | 2016-04-04 | 2017-10-12 | 株式会社エコファースト | ノズル式スチームトラップ |
DE102022131861A1 (de) * | 2022-12-01 | 2024-06-06 | Hps Home Power Solutions Ag | Kondensatablaufeinrichtung und Verfahren zu deren Betrieb |
Family Cites Families (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US426880A (en) * | 1890-04-29 | Steam-separator | ||
US2059521A (en) * | 1936-11-03 | Multistage centrifugal separation | ||
US1533835A (en) * | 1923-11-01 | 1925-04-14 | Clarence A Dawley | Separator and trap |
FR859292A (fr) * | 1939-05-05 | 1940-12-14 | Air Equipement | Perfectionnements aux épurateurs d'air comprimé |
US2726732A (en) * | 1952-07-17 | 1955-12-13 | C A Norgren Company | Air line filter and automatic drain valve |
US2707051A (en) * | 1952-11-03 | 1955-04-26 | Harold J Mailhot | Pressure regulator-filter device |
US3378993A (en) * | 1963-07-03 | 1968-04-23 | Bastian Blessing Co | Air line filter |
GB1096312A (en) * | 1964-01-27 | 1967-12-29 | Exactor Sterling Ltd | Drain valves |
US3269097A (en) * | 1964-01-27 | 1966-08-30 | Aro Corp | Airline filter |
US3418789A (en) * | 1965-08-30 | 1968-12-31 | Norgren Co C A | Automatic liquid discharge mechanism |
US3507098A (en) * | 1966-08-18 | 1970-04-21 | Astro Control Inc | Air line filter |
US3559764A (en) * | 1968-06-05 | 1971-02-02 | Harry L Wheeler Jr | Selective filter, regulator and lubricator component arrangement for air lines |
US3901670A (en) * | 1974-03-07 | 1975-08-26 | Takeshi Minami | Lubricant separating means for air driven machinery |
US3898068A (en) * | 1974-05-31 | 1975-08-05 | John A Mcneil | Cyclonic separator |
US4136009A (en) * | 1977-11-17 | 1979-01-23 | David Samiran | Adjustable float and filter assembly |
US4409005A (en) * | 1981-07-06 | 1983-10-11 | Mckendrick Lorne J | Method and apparatus for separating liquid and solid contaminants from a flowing gas |
NZ209289A (en) * | 1983-10-27 | 1987-03-31 | Tlv Co Ltd | Gas pressure reducing valve with liquid separator |
DE3541370A1 (de) * | 1984-11-23 | 1986-05-28 | Domnick Hunter Filters Ltd., Birtley, Co. Durham | Fluessigkeits/gas-abscheider |
JPS61157914A (ja) * | 1984-12-28 | 1986-07-17 | Tlv Co Ltd | 排水弁付き減圧弁 |
PH24211A (en) * | 1985-02-15 | 1990-04-10 | Takeshi Yokoyama | Gas-water separator |
-
1985
- 1985-09-17 JP JP60205629A patent/JPS6267397A/ja active Granted
-
1986
- 1986-08-12 ZA ZA866051A patent/ZA866051B/xx unknown
- 1986-08-16 CN CN86105071.1A patent/CN1003803B/zh not_active Expired
- 1986-08-26 KR KR1019860007076A patent/KR920008197B1/ko not_active IP Right Cessation
- 1986-09-01 PH PH34207A patent/PH24329A/en unknown
- 1986-09-12 GR GR862338A patent/GR862338B/el unknown
- 1986-09-16 GB GB8622268A patent/GB2189878B/en not_active Expired
- 1986-09-16 CH CH3703/86A patent/CH671086A5/de not_active IP Right Cessation
- 1986-09-16 IT IT21721/86A patent/IT1197232B/it active
- 1986-09-16 CA CA000518285A patent/CA1273262A/en not_active Expired - Lifetime
- 1986-09-16 PT PT83391A patent/PT83391B/pt not_active IP Right Cessation
- 1986-09-16 DE DE8624703U patent/DE8624703U1/de not_active Expired
- 1986-09-17 ES ES8602328A patent/ES2002513A6/es not_active Expired
- 1986-09-17 BE BE2/61054A patent/BE905442A/fr not_active IP Right Cessation
- 1986-09-17 FR FR868613016A patent/FR2587443B1/fr not_active Expired - Lifetime
- 1986-09-17 NZ NZ217606A patent/NZ217606A/xx unknown
-
1987
- 1987-09-10 US US07/097,328 patent/US4867767A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
KR920008197B1 (ko) | 1992-09-25 |
GB8622268D0 (en) | 1986-10-22 |
GR862338B (en) | 1987-01-12 |
DE8624703U1 (de) | 1987-01-15 |
IT1197232B (it) | 1988-11-30 |
NZ217606A (en) | 1988-07-28 |
JPH0314119B2 (zh) | 1991-02-26 |
IT8621721A1 (it) | 1988-03-16 |
GB2189878A (en) | 1987-11-04 |
CH671086A5 (zh) | 1989-07-31 |
JPS6267397A (ja) | 1987-03-27 |
US4867767A (en) | 1989-09-19 |
ZA866051B (en) | 1987-03-25 |
FR2587443B1 (fr) | 1991-10-31 |
KR870002860A (ko) | 1987-04-13 |
PH24329A (en) | 1990-05-29 |
FR2587443A1 (fr) | 1987-03-20 |
BE905442A (fr) | 1987-01-16 |
IT8621721A0 (it) | 1986-09-16 |
ES2002513A6 (es) | 1988-08-16 |
CN86105071A (zh) | 1987-03-18 |
PT83391B (pt) | 1992-10-30 |
CA1273262A (en) | 1990-08-28 |
GB2189878B (en) | 1989-08-23 |
PT83391A (en) | 1986-10-01 |
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