JP2003269400A - Steam ejector device - Google Patents
Steam ejector deviceInfo
- Publication number
- JP2003269400A JP2003269400A JP2002069791A JP2002069791A JP2003269400A JP 2003269400 A JP2003269400 A JP 2003269400A JP 2002069791 A JP2002069791 A JP 2002069791A JP 2002069791 A JP2002069791 A JP 2002069791A JP 2003269400 A JP2003269400 A JP 2003269400A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- pressure
- pipe
- ejector
- delivery pipe
- 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.)
- Pending
Links
- 238000007599 discharging Methods 0.000 claims description 2
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 230000007423 decrease Effects 0.000 description 7
- 238000010586 diagram Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Jet Pumps And Other Pumps (AREA)
Abstract
Description
【発明の詳細な説明】
【0001】
【発明の属する技術分野】本発明は、駆動蒸気と吸入蒸
気が混合されてディフューザから吐出される蒸気エゼク
タに関し、特に、吐出側から安定した圧力状態の蒸気を
吐出することのできる蒸気エゼクタ装置に関する。
【0002】石油・化学プラントや紙・パルプ、繊維工
場あるいは食品工場等の各種の蒸気使用施設において
は、熱エネルギの省エネ化を図るために、一度使用され
た高圧蒸気の再利用や、中・低圧蒸気の活用が行われて
いる。そして、低圧蒸気を回収して活用するものとして
蒸気エゼクタが広く使用されている。
【0003】
【従来技術】従来の蒸気エゼクタ装置としては、例えば
図2に示すものが用いられていた。これは、ノズルを内
蔵した吸引室1とディフューザ2とから成り、圧力調節
弁5を取り付けた高圧の駆動蒸気管3を吸引室1のノズ
ルと接続し、低圧の吸入蒸気管4を吸引室1と接続し
て、ディフューザ2の出口側に吐出管6を接続したもの
で、吐出管6に圧力センサ7を取り付けて圧力調節弁5
と電気的に接続することにより、吐出管6側の蒸気圧力
を所定値範囲に維持して、蒸気エゼクタとしての効率を
高く保持することができるものである。
【0004】
【発明が解決しようとする課題】上記従来の蒸気エゼク
タでは、吐出管6から蒸気使用箇所へ供給される蒸気の
圧力が変動してしまう問題があった。蒸気エゼクタは、
駆動蒸気圧力と吐出蒸気圧力をほぼ一定の所定値に維持
して使用されるのであるが、吸入蒸気が減少したり、あ
るいは、吐出管6側の蒸気使用箇所での蒸気消費量が増
えた時に、圧力調節弁5の弁開度を大きくして供給蒸気
量を増やそうとすると、ある範囲までは供給蒸気量を増
やすことができるが、圧力調節弁5の弁開度が全開にな
った後、更に吸入蒸気が減少したり蒸気使用箇所での蒸
気消費量が増えると、吐出管6側の圧力は低下してしま
う。
【0005】吐出管6側の圧力が低下すると、ここから
供給される蒸気使用箇所での蒸気圧力が変動して、蒸気
温度や伝達熱量が変化して生産物に悪影響を及ぼすので
ある。
【0006】従って本発明の課題は、吐出管6から供給
される蒸気圧力の変動を少なくすることのできる蒸気エ
ゼクタ装置を得ることである。
【0007】
【課題を解決するための手段】上記の課題を解決するた
めに講じた本発明の手段は、駆動蒸気をノズルに供給す
ると共に、吸引室で吸入蒸気を吸引して、当該吸入蒸気
と駆動蒸気の混合蒸気をディフューザから所定箇所へ吐
出する蒸気エゼクタにおいて、蒸気エゼクタにバイパス
路を設けて、当該バイパス路へディフューザからの吐出
蒸気圧力に応じて開閉制御される圧力制御弁を取り付け
たものである。
【0008】
【発明の実施の形態】ディフューザからの吐出蒸気圧力
に応じて開閉制御される圧力制御弁を取り付けたバイパ
ス路を設けたことにより、吐出蒸気圧力が低下すると圧
力制御弁を開弁して高圧蒸気を吐出側へ供給することに
よって圧力の変動を防止することができる。
【0009】
【実施例】図1に示すように、蒸気エゼクタ10と、バ
イパス路11、及び、圧力制御弁12とで蒸気エゼクタ
装置を構成する。なお、従来例と同一部材には同一符号
を付す。
【0010】蒸気エゼクタ10は、内部に図示しないノ
ズルを内蔵した吸引室1とディフューザ2とから成り、
圧力調節弁5を取り付けた高圧の駆動蒸気管3を吸引室
1のノズルと接続する。一方、低圧の吸入蒸気管4も吸
引室1と接続する。ディフューザ2の出口側には吐出管
6を接続して、この吐出管6に管内を通過する蒸気の圧
力を検出する圧力センサ7を取り付ける。吐出管6は図
示しない蒸気使用装置と接続する。また、圧力センサ7
は圧力調節弁5と電気的に接続する。
【0011】駆動蒸気管3を分岐してバイパス路11を
設けて、その出口側を吐出管6と接続する。バイパス路
11の途中に圧力制御弁12を取り付ける。本実施例の
圧力制御弁12としては、自力式調整弁の一種である減
圧弁を用いることができる。
【0012】減圧弁12は、内部にダイヤフラムやベロ
ーズ等の圧力応動部材を有し、減圧弁12の出口側すな
わち吐出管6内側の圧力を圧力応動部材が自動的に検知
して弁体を開閉弁するもので、吐出管6側の圧力が減圧
弁12の設定圧力よりも低下すると自動的に開弁して、
駆動蒸気管3から高圧蒸気を吐出管6側へ供給し、減圧
弁12の出口側圧力が設定圧力と等しくなると自動的に
閉弁して高圧蒸気の供給を停止する。
【0013】本実施例においては、駆動蒸気管3の蒸気
圧力を10kg/cm2、吐出管6内の蒸気圧力を5.
5kg/cm2、及び、減圧弁12の設定圧力を5.0
kg/cm2とする。
【0014】圧力調節弁5を介して駆動蒸気管3から蒸
気エゼクタ10へ高圧の駆動蒸気が供給されて、吸入蒸
気管4から低圧例えば2〜3kg/cm2程度の低圧蒸
気が吸引され、吐出管6から図示しない蒸気使用装置へ
と送られる。この場合、吐出管6側の蒸気圧力が5.5
kg/cm2となるように圧力調節弁5の開度が自動的
に調節される。
【0015】吸入蒸気管4からの低圧蒸気の吸引量が減
少するか、あるいは、吐出管6と接続された蒸気使用装
置での蒸気使用量が増大すると、吐出管6内の蒸気圧力
が低下して、この圧力低下が圧力センサ7で検出され、
圧力調節弁5の弁開度を大きくすることによって、吐出
管6側の蒸気圧力は5.5kg/cm2に維持される。
【0016】しかしながら、圧力調節弁5の弁開度が全
開となった後で、吸入蒸気管4からの低圧蒸気が更に減
少するか、あるいは、蒸気使用装置での蒸気使用量が更
に増大すると、吐出管6側の蒸気圧力は低下してしまう
のであるが、本実施例においては吐出管6側の蒸気圧力
が5.0kg/cm2まで低下すると、バイパス路11
に取り付けた減圧弁12が自動的に開弁してそれ以上の
圧力低下を防止する。
【0017】本実施例においては、減圧弁12の設定圧
力を5.0として、吐出管6内の蒸気圧力が5.5から
0.5kg/cm2低下すると減圧弁12が開弁する例
を示したが、減圧弁12の設定圧力を5.5へ近づける
ことによって、吐出管6内の蒸気圧力の変動を更に小さ
な値とすることができる。
【0018】また、本実施例においては圧力制御弁とし
て減圧弁12を用いた例を示したが、圧力調節弁5と同
じく他力式自動弁の一種である自動調節弁を圧力センサ
7と組み合わせて用いることもできる。
【0019】
【発明の効果】本発明によれば、蒸気エゼクタにバイパ
ス路を設けて、ディフューザからの吐出蒸気圧力に応じ
て開閉制御される圧力制御弁を取り付けたことにより、
吐出管から供給される蒸気圧力の変動を少なくすること
ができる。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam ejector in which a driving steam and a suction steam are mixed and discharged from a diffuser, and more particularly, to a steam having a stable pressure state from a discharge side. The present invention relates to a steam ejector device capable of discharging water. [0002] In various steam-using facilities such as petroleum and chemical plants, paper and pulp, textile factories and food factories, in order to save heat energy, it is necessary to reuse high-pressure steam once used and to reduce Utilization of low pressure steam is being carried out. A steam ejector is widely used for recovering and utilizing low-pressure steam. As a conventional steam ejector, for example, the one shown in FIG. 2 has been used. It comprises a suction chamber 1 with a built-in nozzle and a diffuser 2. A high-pressure driving steam pipe 3 equipped with a pressure control valve 5 is connected to the nozzle of the suction chamber 1, and a low-pressure suction steam pipe 4 is connected to the suction chamber 1. And a discharge pipe 6 connected to the outlet side of the diffuser 2. A pressure sensor 7 is attached to the discharge pipe 6 to
By electrically connecting the steam ejector, the steam pressure on the discharge pipe 6 side can be maintained within a predetermined value range, and the efficiency as a steam ejector can be kept high. [0004] The above-mentioned conventional steam ejector has a problem that the pressure of the steam supplied from the discharge pipe 6 to the location where the steam is used fluctuates. The steam ejector
The driving steam pressure and the discharge steam pressure are used while being maintained at substantially constant predetermined values. However, when the intake steam decreases or the steam consumption at the steam use point on the discharge pipe 6 side increases. In order to increase the supply steam amount by increasing the valve opening of the pressure control valve 5, the supply steam amount can be increased up to a certain range, but after the valve opening of the pressure control valve 5 is fully opened, Further, when the amount of steam to be inhaled is reduced or the amount of steam consumed at the location where steam is used increases, the pressure on the discharge pipe 6 side decreases. [0005] When the pressure on the discharge pipe 6 side is reduced, the steam pressure at the point of use of steam supplied from the outlet fluctuates, and the steam temperature and the amount of heat transferred change to adversely affect the product. [0006] Therefore, an object of the present invention is to provide a steam ejector device capable of reducing fluctuations in the steam pressure supplied from the discharge pipe 6. [0007] In order to solve the above-mentioned problems, the means of the present invention is to supply driving steam to a nozzle, suck suction steam in a suction chamber, and supply the suction steam. In a steam ejector that discharges a mixed steam of steam and driving steam from a diffuser to a predetermined location, a bypass passage is provided in the steam ejector, and a pressure control valve that is controlled to open and close according to the steam pressure discharged from the diffuser is attached to the bypass passage. Things. [0008] By providing a bypass with a pressure control valve that is opened and closed according to the pressure of the steam discharged from the diffuser, the pressure control valve is opened when the pressure of the discharged steam decreases. By supplying high-pressure steam to the discharge side, pressure fluctuation can be prevented. As shown in FIG. 1, a steam ejector, a bypass passage 11, and a pressure control valve 12 constitute a steam ejector device. The same members as those in the conventional example are denoted by the same reference numerals. The steam ejector 10 comprises a suction chamber 1 having a nozzle (not shown) therein and a diffuser 2 therein.
The high-pressure driving steam pipe 3 to which the pressure control valve 5 is attached is connected to the nozzle of the suction chamber 1. On the other hand, the low-pressure suction steam pipe 4 is also connected to the suction chamber 1. A discharge pipe 6 is connected to the outlet side of the diffuser 2, and a pressure sensor 7 for detecting the pressure of steam passing through the pipe is attached to the discharge pipe 6. The discharge pipe 6 is connected to a steam using device (not shown). The pressure sensor 7
Is electrically connected to the pressure control valve 5. The driving steam pipe 3 is branched to provide a bypass 11, and the outlet side thereof is connected to the discharge pipe 6. A pressure control valve 12 is attached in the middle of the bypass 11. As the pressure control valve 12 of the present embodiment, a pressure reducing valve which is a kind of a self-powered adjusting valve can be used. The pressure reducing valve 12 has a pressure responsive member such as a diaphragm or a bellows inside. The pressure responsive member automatically detects the pressure on the outlet side of the pressure reducing valve 12, ie, the pressure inside the discharge pipe 6, and opens and closes the valve body. When the pressure on the discharge pipe 6 side falls below the set pressure of the pressure reducing valve 12, the valve opens automatically,
The high-pressure steam is supplied from the driving steam pipe 3 to the discharge pipe 6 side, and when the outlet pressure of the pressure reducing valve 12 becomes equal to the set pressure, the valve is automatically closed to stop the supply of the high-pressure steam. In this embodiment, the steam pressure of the driving steam pipe 3 is 10 kg / cm 2, and the steam pressure of the discharge pipe 6 is 5.
5 kg / cm 2, and the set pressure of the pressure reducing valve 12 is 5.0
kg / cm2. A high-pressure drive steam is supplied from the drive steam pipe 3 to the steam ejector 10 via the pressure control valve 5, and a low-pressure steam of a low pressure of, for example, about 2 to 3 kg / cm 2 is sucked from the suction steam pipe 4 and discharged. From 6 is sent to a steam-using device (not shown). In this case, the steam pressure on the discharge pipe 6 side is 5.5
The opening degree of the pressure control valve 5 is automatically adjusted so as to be kg / cm2. When the amount of low-pressure steam sucked from the suction steam pipe 4 decreases or the amount of steam used in the steam-using device connected to the discharge pipe 6 increases, the steam pressure in the discharge pipe 6 decreases. This pressure drop is detected by the pressure sensor 7,
By increasing the valve opening of the pressure control valve 5, the steam pressure on the discharge pipe 6 side is maintained at 5.5 kg / cm2. However, if the low-pressure steam from the suction steam pipe 4 further decreases or the amount of steam used in the steam-using device further increases after the valve opening of the pressure control valve 5 is fully opened, Although the steam pressure on the discharge pipe 6 side drops, in this embodiment, when the steam pressure on the discharge pipe 6 side drops to 5.0 kg / cm 2, the bypass passage 11
The pressure reducing valve 12 attached to the valve automatically opens to prevent a further pressure drop. In the present embodiment, an example is shown in which the set pressure of the pressure reducing valve 12 is set to 5.0 and the pressure reducing valve 12 is opened when the steam pressure in the discharge pipe 6 decreases from 5.5 to 0.5 kg / cm 2. However, by making the set pressure of the pressure reducing valve 12 close to 5.5, the fluctuation of the steam pressure in the discharge pipe 6 can be made smaller. Further, in this embodiment, an example in which the pressure reducing valve 12 is used as the pressure control valve is shown. Can also be used. According to the present invention, a bypass path is provided in a steam ejector, and a pressure control valve that is controlled to open and close according to a steam pressure discharged from a diffuser is attached.
Fluctuation in the steam pressure supplied from the discharge pipe can be reduced.
【図面の簡単な説明】
【図1】本発明の蒸気エゼクタ装置の実施例を示す構成
図。
【図2】蒸気エゼクタ装置の従来例を示す構成図。
【符号の説明】
1 吸引室
2 ディフューザ
3 駆動蒸気管
4 吸入蒸気管
5 圧力調節弁
6 吐出管
7 圧力センサ
10 蒸気エゼクタ
11 バイパス路
12 圧力制御弁
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a configuration diagram showing an embodiment of a steam ejector device of the present invention. FIG. 2 is a configuration diagram showing a conventional example of a steam ejector device. [Description of Signs] 1 suction chamber 2 diffuser 3 drive steam pipe 4 suction steam pipe 5 pressure control valve 6 discharge pipe 7 pressure sensor 10 steam ejector 11 bypass passage 12 pressure control valve
Claims (1)
引室で吸入蒸気を吸引して、当該吸入蒸気と駆動蒸気の
混合蒸気をディフューザから所定箇所へ吐出する蒸気エ
ゼクタにおいて、蒸気エゼクタにバイパス路を設けて、
当該バイパス路へディフューザからの吐出蒸気圧力に応
じて開閉制御される圧力制御弁を取り付けたことを特徴
とする蒸気エゼクタ装置。Claims: 1. A steam ejector for supplying a driving steam to a nozzle, sucking a suction steam in a suction chamber, and discharging a mixed steam of the suction steam and the driving steam from a diffuser to a predetermined location. , By installing a bypass in the steam ejector,
A steam ejector device, wherein a pressure control valve that is opened and closed according to the steam pressure discharged from a diffuser is attached to the bypass passage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002069791A JP2003269400A (en) | 2002-03-14 | 2002-03-14 | Steam ejector device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002069791A JP2003269400A (en) | 2002-03-14 | 2002-03-14 | Steam ejector device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2003269400A true JP2003269400A (en) | 2003-09-25 |
Family
ID=29200532
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2002069791A Pending JP2003269400A (en) | 2002-03-14 | 2002-03-14 | Steam ejector device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2003269400A (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007218471A (en) * | 2006-02-15 | 2007-08-30 | Tlv Co Ltd | Waste heat-recovering/pressure-reducing device for steam |
| JP2007218474A (en) * | 2006-02-15 | 2007-08-30 | Tlv Co Ltd | Waste heat-recovering/pressure-reducing device for steam |
| JP2007218473A (en) * | 2006-02-15 | 2007-08-30 | Tlv Co Ltd | Waste heat-recovering/pressure-reducing device for steam |
| JP2007218472A (en) * | 2006-02-15 | 2007-08-30 | Tlv Co Ltd | Waste heat-recovering/pressure-reducing device for steam |
| JP2007332860A (en) * | 2006-06-15 | 2007-12-27 | Tlv Co Ltd | Steam ejector |
| JP2007332859A (en) * | 2006-06-15 | 2007-12-27 | Tlv Co Ltd | Steam ejector |
| JP2007332861A (en) * | 2006-06-15 | 2007-12-27 | Tlv Co Ltd | Steam ejector |
| JP2008019814A (en) * | 2006-07-14 | 2008-01-31 | Tlv Co Ltd | Steam ejector |
| JP2008150996A (en) * | 2006-12-15 | 2008-07-03 | Tlv Co Ltd | Steam ejector |
| JP2008150995A (en) * | 2006-12-15 | 2008-07-03 | Tlv Co Ltd | Steam ejector |
| JP2009144609A (en) * | 2007-12-14 | 2009-07-02 | Tlv Co Ltd | Steam ejector |
| US20220152883A1 (en) * | 2019-03-28 | 2022-05-19 | Philip Morris Products S.A. | Forming apparatus and method for forming a continuous tubular rod |
| JP7528044B2 (en) | 2021-09-24 | 2024-08-05 | 北海道瓦斯株式会社 | Gas Supply System |
-
2002
- 2002-03-14 JP JP2002069791A patent/JP2003269400A/en active Pending
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007218471A (en) * | 2006-02-15 | 2007-08-30 | Tlv Co Ltd | Waste heat-recovering/pressure-reducing device for steam |
| JP2007218474A (en) * | 2006-02-15 | 2007-08-30 | Tlv Co Ltd | Waste heat-recovering/pressure-reducing device for steam |
| JP2007218473A (en) * | 2006-02-15 | 2007-08-30 | Tlv Co Ltd | Waste heat-recovering/pressure-reducing device for steam |
| JP2007218472A (en) * | 2006-02-15 | 2007-08-30 | Tlv Co Ltd | Waste heat-recovering/pressure-reducing device for steam |
| JP2007332861A (en) * | 2006-06-15 | 2007-12-27 | Tlv Co Ltd | Steam ejector |
| JP2007332859A (en) * | 2006-06-15 | 2007-12-27 | Tlv Co Ltd | Steam ejector |
| JP2007332860A (en) * | 2006-06-15 | 2007-12-27 | Tlv Co Ltd | Steam ejector |
| JP2008019814A (en) * | 2006-07-14 | 2008-01-31 | Tlv Co Ltd | Steam ejector |
| JP2008150996A (en) * | 2006-12-15 | 2008-07-03 | Tlv Co Ltd | Steam ejector |
| JP2008150995A (en) * | 2006-12-15 | 2008-07-03 | Tlv Co Ltd | Steam ejector |
| JP2009144609A (en) * | 2007-12-14 | 2009-07-02 | Tlv Co Ltd | Steam ejector |
| US20220152883A1 (en) * | 2019-03-28 | 2022-05-19 | Philip Morris Products S.A. | Forming apparatus and method for forming a continuous tubular rod |
| US12427700B2 (en) * | 2019-03-28 | 2025-09-30 | Philip Morris Products S.A. | Forming apparatus and method for forming a continuous tubular rod |
| JP7528044B2 (en) | 2021-09-24 | 2024-08-05 | 北海道瓦斯株式会社 | Gas Supply System |
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