JP5065138B2 - Condensate pumping device - Google Patents

Condensate pumping device Download PDF

Info

Publication number
JP5065138B2
JP5065138B2 JP2008105928A JP2008105928A JP5065138B2 JP 5065138 B2 JP5065138 B2 JP 5065138B2 JP 2008105928 A JP2008105928 A JP 2008105928A JP 2008105928 A JP2008105928 A JP 2008105928A JP 5065138 B2 JP5065138 B2 JP 5065138B2
Authority
JP
Japan
Prior art keywords
condensate
working steam
steam
inlet
working
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
JP2008105928A
Other languages
Japanese (ja)
Other versions
JP2009257160A (en
Inventor
広谷  昌久
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tlv Co Ltd
Original Assignee
Tlv Co Ltd
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 Tlv Co Ltd filed Critical Tlv Co Ltd
Priority to JP2008105928A priority Critical patent/JP5065138B2/en
Publication of JP2009257160A publication Critical patent/JP2009257160A/en
Application granted granted Critical
Publication of JP5065138B2 publication Critical patent/JP5065138B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Jet Pumps And Other Pumps (AREA)

Description

本発明は、各種蒸気使用装置で発生した復水をボイラーや廃熱利用箇所に圧送する復水圧送装置に関するものである。   The present invention relates to a condensate pumping device that pumps condensate generated in various steam using devices to a boiler or a waste heat utilization site.

従来の復水圧送装置は、作動蒸気導入口と作動蒸気排出口と圧送復水流入口及び圧送復水排出口が設けられた密閉容器の内部の復水溜空間にフロートと切替え弁が配置され、フロートの昇降に応じて切替え弁で作動蒸気導入口と作動蒸気排出口の開閉を切り換えて、初めに作動蒸気排出口を開き作動蒸気導入口を閉じて圧送復水流入口から復水溜空間に復水を流入させ、次いで作動蒸気排出口を閉じ作動蒸気導入口を開いて復水溜空間に溜った復水を圧送復水排出口から圧送するものである。   In the conventional condensate pressure feeding device, a float and a switching valve are arranged in a condensate reservoir space inside a sealed container provided with a working steam inlet, a working steam outlet, a pressure condensate inlet and a pressure condensate outlet, The switching valve opens and closes the opening and closing of the working steam inlet and the working steam outlet, and first opens the working steam outlet and closes the working steam inlet, and then condenses the condensate from the condensate condensate inlet to the condensate reservoir space. Then, the working steam discharge port is closed, the working steam introduction port is opened, and the condensate accumulated in the condensate reservoir space is pumped from the condensate discharge port.

上記従来の復水圧送装置は、作動蒸気導入口へ供給される作動蒸気の保有する熱量を有効に活用することができないという問題点があった。
特開平9−53794
The conventional condensate pressure feeding device has a problem in that it cannot effectively utilize the amount of heat held by the working steam supplied to the working steam inlet.
JP-A-9-53794

解決しようとする課題は、作動蒸気導入口へ供給される作動蒸気の保有する熱量を有効に活用することのできる復水圧送装置を提供することである。   The problem to be solved is to provide a condensate pressure feeding device capable of effectively utilizing the amount of heat held by the working steam supplied to the working steam inlet.

本発明は、作動蒸気導入口と作動蒸気排出口と圧送復水流入口及び圧送復水排出口が設けられた密閉容器内の復水溜空間にフロートと切替え弁が配置され、フロートの昇降に応じて切替え弁で作動蒸気導入口と作動蒸気排出口の開閉を切り換えて、初めに作動蒸気排出口を開き作動蒸気導入口を閉じて圧送復水流入口から復水溜空間に復水を流入させ、次いで作動蒸気排出口を閉じ作動蒸気導入口を開いて復水溜空間に溜った復水を圧送復水排出口から圧送する復水圧送装置において、作動蒸気導入口に作動蒸気を供給する作動蒸気供給管を接続して、当該作動蒸気供給管に第一の熱交換部材を取り付けると共に、作動蒸気排出口に作動蒸気を排出する作動蒸気排出管を接続して、当該作動蒸気排出管に第二の熱交換部材を取り付けて、当該第一及び第二の熱交換部材で作動蒸気と別途の流体とを熱交換するものである。   In the present invention, a float and a switching valve are arranged in a condensate reservoir space in a sealed container provided with a working steam inlet, a working steam outlet, a pressure condensate inlet, and a pressure condensate outlet, Switch the opening and closing of the working steam inlet and the working steam outlet with the switching valve, open the working steam outlet first, close the working steam inlet and let the condensate flow into the condensate reservoir space from the pressure condensate inlet, then operate In the condensate pressure feeding device that closes the steam outlet and opens the working steam inlet and pumps the condensate collected in the condensate reservoir space from the pressure condensate outlet, the working steam supply pipe that supplies the working steam to the working steam inlet Connect the first heat exchange member to the working steam supply pipe, connect the working steam discharge pipe for discharging the working steam to the working steam discharge port, and connect the second heat exchange to the working steam discharge pipe. Attach the member A separate fluid and the working steam with first and second heat exchange member is for heat exchange.

本発明の復水圧送装置は、作動蒸気導入口に接続した作動蒸気供給管に熱交換部材を取り付けて、この熱交換部材で作動蒸気と別途の流体とを熱交換することにより、作動蒸気の保有する熱量を有効に活用することができるという優れた効果を生じる。   The condensate pressure feeding device of the present invention attaches a heat exchange member to a working steam supply pipe connected to the working steam inlet, and exchanges heat between the working steam and a separate fluid by this heat exchange member. An excellent effect is obtained that the amount of heat held can be effectively utilized.

本発明は、作動蒸気供給管に熱交換部材を取り付けるものであるが、熱交換部材としては、従来公知のものを用いることができ、例えば、常温水と高温の作動蒸気が間接的に熱交換されて、作動蒸気の温度が低下すると共に、常温水の温度を上昇させるタイプの熱交換部材が好適である。   In the present invention, a heat exchange member is attached to a working steam supply pipe, and a conventionally known heat exchange member can be used as the heat exchange member. For example, room temperature water and high temperature working steam indirectly exchange heat. Thus, a type of heat exchange member that lowers the temperature of the working steam and raises the temperature of the room temperature water is suitable.

本実施例においては、蒸気と水の熱交換器1で発生した復水を、復水タンク2を介して復水圧送装置3で所定箇所へ圧送する復水圧送装置の例を示す。   In the present embodiment, an example of a condensate pumping device that pumps the condensate generated in the heat exchanger 1 for steam and water to a predetermined location by the condensate pumping device 3 through the condensate tank 2 is shown.

熱交換器1に蒸気供給管4と水供給管5を、それぞれ平行に取り付ける。蒸気供給管4から供給される蒸気と、水供給管5から供給される水が、熱交換器1内で熱交換されて、所定温度まで温度上昇した温水が、温水排出管6から所定箇所へ排出されるものである。   A steam supply pipe 4 and a water supply pipe 5 are attached to the heat exchanger 1 in parallel. Steam supplied from the steam supply pipe 4 and water supplied from the water supply pipe 5 are heat-exchanged in the heat exchanger 1, and hot water whose temperature has risen to a predetermined temperature is transferred from the hot water discharge pipe 6 to a predetermined location. It will be discharged.

蒸気供給管4を分岐して分岐蒸気供給管7を接続する。分岐蒸気供給管7に第一の熱交換部材8を取り付けて、下端を復水圧送装置3の作動蒸気導入口13と接続する。第一の熱交換部材8は、左側に水供給管5を接続して、右側に第二の熱交換部材9を介在して熱交換器1と接続する。   The steam supply pipe 4 is branched and a branch steam supply pipe 7 is connected. The first heat exchange member 8 is attached to the branch steam supply pipe 7, and the lower end is connected to the working steam inlet 13 of the condensate pump 3. The first heat exchange member 8 is connected to the heat exchanger 1 via the water supply pipe 5 on the left side and the second heat exchange member 9 on the right side.

第一の熱交換部材8と作動蒸気導入口13の間の分岐蒸気供給管7を更に分岐して分岐管10を延長して蒸気トラップ11を取り付ける。蒸気トラップ11は、分岐蒸気供給管7内を流下してくる復水と蒸気の混合流体の内で、復水だけを自動的に外部に排出して、蒸気は外部へ排出することのないものである。   The branch steam supply pipe 7 between the first heat exchange member 8 and the working steam inlet 13 is further branched, the branch pipe 10 is extended, and the steam trap 11 is attached. The steam trap 11 automatically discharges only the condensate out of the condensate / steam mixed fluid flowing down in the branch steam supply pipe 7 and does not discharge the steam to the outside. It is.

第二の熱交換部材9の上部と、復水圧送装置3の作動蒸気排出口14とを作動蒸気排出管12で接続する。第二の熱交換部材9の下部は、管路15で復水タンク2と接続する。   The upper part of the second heat exchange member 9 and the working steam discharge port 14 of the condensate pump 3 are connected by a working steam discharge pipe 12. The lower part of the second heat exchange member 9 is connected to the condensate tank 2 by a pipe line 15.

復水圧送装置3の圧送復水流入口16と、復水タンク2とを連通管17で連通する。復水圧送装置3は、圧送復水流入口16と圧送復水排出口18、及び、高圧の作動蒸気導入口13と作動蒸気排出口14を有し、圧送復水流入口16に逆止弁19を介して連通管17を接続する。逆止弁19は、連通管17から復水圧送装置3内への液体の流下は許容し、反対の液体流れは阻止するものである。同様に、圧送復水排出口18に逆止弁20を介して復水圧送管21を接続する。この逆止弁20は、復水圧送装置3から復水圧送管21への液体の流下を許容し、反対の流れは阻止する機能を有する。 A pressure condensate inlet 16 of the condensate pressure feeding device 3 communicates with the condensate tank 2 through a communication pipe 17. The condensate pressure feeding device 3 has a pressure condensate condensate inlet 16 and a pressure condensate discharge port 18, and a high pressure working steam inlet 13 and a working steam discharge port 14. A check valve 19 is provided at the pressure condensate inlet 16. The communication pipe 17 is connected via The check valve 19 allows the liquid to flow from the communication pipe 17 into the condensate pressure feeding device 3 and blocks the opposite liquid flow. Similarly, a condensate pressure feed pipe 21 is connected to the pressure feed condensate discharge port 18 via a check valve 20. The check valve 20 has a function of allowing the liquid to flow from the condensate pressure feeding device 3 to the condensate pressure feeding pipe 21 and blocking the opposite flow.

復水圧送装置3は、内部に配置した図示しないフロートが下方部に位置する場合に、作動蒸気導入口13を閉口し、一方、作動蒸気排出口14を開口して、連通管17から復水タンク2内の復水を逆止弁19と圧送復水流入口16を通して復水圧送装置3内に流下させるものである。 The condensate pressure feeding device 3 closes the working steam inlet 13 and opens the working steam outlet 14 when the float (not shown) disposed inside is located in the lower part, and condensates from the communication pipe 17. The condensate in the tank 2 is caused to flow down into the condensate pressure feeding device 3 through the check valve 19 and the pressure condensate inlet 16.

復水圧送装置3内に復水が溜って図示しないフロートが所定上方部に位置すると、作動蒸気排出口14を閉口し、作動蒸気導入口13を開口して、分岐蒸気供給管7から高圧蒸気を復水圧送装置3の内部に流入させることにより、内部に溜った復水を圧送復水流出口18と逆止弁20と復水圧送管21を通して所定箇所へ圧送する。 When condensate accumulates in the condensate pump 3 and a float (not shown) is positioned at a predetermined upper portion, the working steam discharge port 14 is closed, the working steam introduction port 13 is opened, and the high pressure steam is supplied from the branch steam supply pipe 7. Is fed into the condensate pressure feeding device 3 to pump the condensate accumulated therein to a predetermined location through the pressure feed condensate outlet 18, the check valve 20, and the condensate pressure feed pipe 21.

復水が圧送されて復水圧送装置3内の水位が低下すると、再度、作動蒸気導入口13を閉口し、作動蒸気排出口14を開口することにより、圧送復水流入口16から復水を内部へ流下させる。このような作動サイクルを繰り返すことにより、復水圧送装置3は、連通管17からの復水を所定箇所へ圧送する。   When the condensate is pumped and the water level in the condensate pumping device 3 decreases, the working steam inlet 13 is closed again and the working steam discharge port 14 is opened, so that the condensate is introduced into the condensate condensate inlet 16 from the inside. Flow down. By repeating such an operation cycle, the condensate pressure feeding device 3 pressure-feeds the condensate from the communication pipe 17 to a predetermined location.

蒸気供給管4と分岐蒸気供給管7から第一の熱交換部材8へ供給される蒸気の一部は、水供給管5から供給される水と熱交換して、水を昇温させる。水を昇温させることにより熱を奪われた一部の蒸気は凝縮して復水となり、蒸気トラップ11から外部へ排出される。蒸気トラップ11で復水の排出された残余の蒸気は、作動蒸気導入口13から復水圧送装置3へ供給される。   A part of the steam supplied from the steam supply pipe 4 and the branched steam supply pipe 7 to the first heat exchange member 8 exchanges heat with the water supplied from the water supply pipe 5 to raise the temperature of the water. A part of the steam deprived of heat by raising the temperature of the water condenses and becomes condensed water, and is discharged from the steam trap 11 to the outside. The remaining steam discharged from the condensate by the steam trap 11 is supplied from the working steam inlet 13 to the condensate pressure feeding device 3.

復水圧送装置3の作動蒸気排出口14から排出される蒸気は、第二の熱交換部材9で、水供給管5から供給される水を更に加熱して昇温させる。水を昇温して凝縮した復水は管路15を通って復水タンク2へ流下する。   The steam discharged from the working steam outlet 14 of the condensate pressure feeding device 3 is heated by the second heat exchange member 9 by further heating the water supplied from the water supply pipe 5. Condensate condensed by heating the water flows down to the condensate tank 2 through the pipe 15.

分岐蒸気供給管7から作動蒸気導入口13へ供給される蒸気の一部の熱量、及び、作動蒸気排出口14から排出される作動蒸気の熱量で、水供給管5を通過する水を所定温度まで昇温させることができ、作動蒸気の保有する熱量を有効に活用することができる。   The water passing through the water supply pipe 5 is heated at a predetermined temperature by the heat amount of a part of the steam supplied from the branch steam supply pipe 7 to the working steam inlet 13 and the heat quantity of the working steam discharged from the working steam outlet 14. It is possible to raise the temperature up to a maximum, and the amount of heat held by the working steam can be used effectively.

本発明の復水圧送装置の実施例を示す構成図。The block diagram which shows the Example of the condensate pressure feeding apparatus of this invention.

符号の説明Explanation of symbols

1 熱交換器
2 復水タンク
3 復水圧送装置
4 蒸気供給管
5 水供給管
6 温水排出管
7 分岐蒸気供給管
8 第一の熱交換部材
9 第二の熱交換部材
11 蒸気トラップ
12 作動蒸気排出管
13 作動蒸気導入口
14 作動蒸気排出口
16 圧送復水流入口
17 圧送復水排出口
21 復水圧送管
DESCRIPTION OF SYMBOLS 1 Heat exchanger 2 Condensate tank 3 Condensate pumping device 4 Steam supply pipe 5 Water supply pipe 6 Hot water discharge pipe 7 Branch steam supply pipe 8 1st heat exchange member 9 2nd heat exchange member 11 Steam trap 12 Working steam Discharge pipe 13 Working steam inlet 14 Working steam discharge 16 Pressure condensate inlet 17 Pressure condensate discharge 21 Condensate pressure feed pipe

Claims (1)

作動蒸気導入口と作動蒸気排出口と圧送復水流入口及び圧送復水排出口が設けられた密閉容器内の復水溜空間にフロートと切替え弁が配置され、フロートの昇降に応じて切替え弁で作動蒸気導入口と作動蒸気排出口の開閉を切り換えて、初めに作動蒸気排出口を開き作動蒸気導入口を閉じて圧送復水流入口から復水溜空間に復水を流入させ、次いで作動蒸気排出口を閉じ作動蒸気導入口を開いて復水溜空間に溜った復水を圧送復水排出口から圧送する復水圧送装置において、作動蒸気導入口に作動蒸気を供給する作動蒸気供給管を接続して、当該作動蒸気供給管に第一の熱交換部材を取り付けると共に、作動蒸気排出口に作動蒸気を排出する作動蒸気排出管を接続して、当該作動蒸気排出管に第二の熱交換部材を取り付けて、当該第一及び第二の熱交換部材で作動蒸気と別途の流体とを熱交換することを特徴とする復水圧送装置。
Float and switching valve are arranged in the condensate reservoir space in the closed vessel provided with working steam inlet, working steam outlet, pressure condensate condensate inlet and pressure condensate condensate outlet. Switch between opening and closing the steam inlet and the working steam outlet, first open the working steam outlet, close the working steam inlet, let the condensate flow into the condensate reservoir space from the pressure feed condensate inlet, and then open the working steam outlet In the condensate pressure feeding device that pressurizes the condensate accumulated in the condensate reservoir space by opening the closed working steam introduction port, and connecting the working steam supply pipe for supplying the working steam to the working steam introduction port, The first heat exchange member is attached to the working steam supply pipe, the working steam discharge pipe for discharging the working steam is connected to the working steam discharge port, and the second heat exchange member is attached to the working steam discharge pipe. The first and the second Condensate water pressure feeding apparatus of the of working steam with heat exchange member and a separate fluid, characterized in that the heat exchange.
JP2008105928A 2008-04-15 2008-04-15 Condensate pumping device Expired - Fee Related JP5065138B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2008105928A JP5065138B2 (en) 2008-04-15 2008-04-15 Condensate pumping device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2008105928A JP5065138B2 (en) 2008-04-15 2008-04-15 Condensate pumping device

Publications (2)

Publication Number Publication Date
JP2009257160A JP2009257160A (en) 2009-11-05
JP5065138B2 true JP5065138B2 (en) 2012-10-31

Family

ID=41384892

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2008105928A Expired - Fee Related JP5065138B2 (en) 2008-04-15 2008-04-15 Condensate pumping device

Country Status (1)

Country Link
JP (1) JP5065138B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6022233B2 (en) * 2012-06-28 2016-11-09 株式会社テイエルブイ Condensate recovery device
CN111928062A (en) * 2020-08-18 2020-11-13 江苏华昌化工股份有限公司 Recycling method for byproduct steam of coal gasification conversion device

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3536429B2 (en) * 1995-05-15 2004-06-07 嘉夫 森口 Steam drain recovery device
JPH0953794A (en) * 1995-08-11 1997-02-25 Tlv Co Ltd Condensation forcibly feeding device
JP3895423B2 (en) * 1997-03-14 2007-03-22 株式会社テイエルブイ Liquid pumping device
JP2006226141A (en) * 2005-02-15 2006-08-31 Tlv Co Ltd Condensate pressure feeding device
JP2007205169A (en) * 2006-01-31 2007-08-16 Hitachi Ltd Energy supply system and energy supply method
JP2007247974A (en) * 2006-03-16 2007-09-27 Tlv Co Ltd Steam waste heat recovery device

Also Published As

Publication number Publication date
JP2009257160A (en) 2009-11-05

Similar Documents

Publication Publication Date Title
KR101585898B1 (en) Hot water generator
CN101377346B (en) Ejecting type non-bearing double-temperature water outlet heater
JP5065138B2 (en) Condensate pumping device
JP2013108637A (en) Heat exchanger
JP5393993B2 (en) Condensate pumping device
JP5393994B2 (en) Condensate pumping device
JP6006980B2 (en) Condensate recovery device
JP6809907B2 (en) Drain pot and drain collection system
JP4949770B2 (en) Condensate recovery device
JP4594270B2 (en) Heat exchanger
JP5188831B2 (en) Vacuum steam heater
JP5384152B2 (en) Air heater
JP2008170126A (en) Condensate collecting apparatus
JP4964831B2 (en) Hot water generator
JP5350057B2 (en) Heat exchanger
JP5973199B2 (en) Steam heating device
JP5894862B2 (en) Hot water generator
JP6345382B2 (en) Heat exchanger
JP5855929B2 (en) Heat exchanger
JP5138334B2 (en) Liquid pumping device with foreign matter separation tank
JP4954637B2 (en) Condensate recovery device
JP6006979B2 (en) Condensate recovery device
JP5384151B2 (en) Heat exchanger
JP5236360B2 (en) Hot water generator
JP5457731B2 (en) Heat exchanger

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20110321

TRDD Decision of grant or rejection written
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20120731

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20120807

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20120809

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

Ref document number: 5065138

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20150817

Year of fee payment: 3

LAPS Cancellation because of no payment of annual fees