CN202719899U - Jet type low-pressure waste steam recovery device - Google Patents

Jet type low-pressure waste steam recovery device Download PDF

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Publication number
CN202719899U
CN202719899U CN 201220337866 CN201220337866U CN202719899U CN 202719899 U CN202719899 U CN 202719899U CN 201220337866 CN201220337866 CN 201220337866 CN 201220337866 U CN201220337866 U CN 201220337866U CN 202719899 U CN202719899 U CN 202719899U
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China
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low pressure
chamber
suction chamber
nozzle
mixing chamber
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Expired - Fee Related
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CN 201220337866
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Chinese (zh)
Inventor
王军
王永利
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Individual
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Individual
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Priority to CN 201220337866 priority Critical patent/CN202719899U/en
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Abstract

The utility model discloses a jet type low-pressure waste steam recovery device, which comprises a suction-in chamber, a mixing chamber, a nozzle, a low-pressure waste steam inlet, a cooling water inlet and a hot water outlet, wherein the low-pressure waste steam inlet is communicated with the suction-in chamber; the nozzle is formed in the suction-in chamber, and is connected with the inlet end of the suction-in chamber; the cooling water inlet is communicated with the inlet end of the nozzle; the outlet end of the suction-in chamber is communicated with the inlet end of the mixing chamber; and the outlet end of the mixing chamber is communicated with a hot water outlet. The device is simple in structure, rational in design, convenient to operate, is used safely and reliably, and has high economic benefits and comprehensive social benefits, and low-pressure waste steam can be effectively recycled to meet production requirements.

Description

Injecting type low pressure steam exhaust recovering device
Technical field
The utility model relates to a kind of low-pressure gas retracting device, especially relates to a kind of injecting type low pressure steam exhaust recovering device.
Background technology
The low pressure exhaust steam refers to the steam of low parameter or the low-pressure steam that turbine is got rid of.At present, the low pressure exhaust steam normally slatterns it discharged to atmosphere.Along with world energy sources day is becoming tight, domestic coal price goes up increasingly, it is more urgent that energy savings seems under existing conditions, meanwhile we also see, a large amount of Industrial Boilers, the station boiler equipment such as oxygen-eliminating device, regular unloading container, hydrophobic development unit in running all produce in a large number the low-pressure steams with certain heat energy to the sky discharging, and industrial and mining enterprises in the process of using steam because technological reason also has considerable to the exhaust steam of sky discharging low pressure.These energy with recoverable value can not get effective utilization for a long time, and energy waste is serious.For this reason, increasingly under the intense situation, it is very necessary that the low pressure exhaust steam is reclaimed at the current energy.
The utility model content
The purpose of this utility model is to overcome above-mentioned deficiency of the prior art, a kind of injecting type low pressure steam exhaust recovering device is provided, it is simple in structure, reasonable in design and use easy and simple to handle, can effectively realize the recycling to the low pressure exhaust steam, to satisfy Production requirement, simultaneously safe and reliable, economic benefit is high, and social synthesis is profitable.
For achieving the above object, the technical solution adopted in the utility model is: a kind of injecting type low pressure steam exhaust recovering device is characterized in that: comprise suction chamber, mixing chamber, nozzle, low pressure exhaust steam entrance, cold water inlet and hot water outlet; Described low pressure exhaust steam entrance is connected with suction chamber, described nozzle is arranged on the inside of suction chamber and is connected with the arrival end of suction chamber, described cold water inlet is connected with the arrival end of nozzle, the port of export of described suction chamber is connected with the arrival end of mixing chamber, and the port of export of described mixing chamber is connected with hot water outlet.
Above-mentioned injecting type low pressure steam exhaust recovering device is characterized in that: the port of export of described mixing chamber is diffuser and is horn-like.
Above-mentioned injecting type low pressure steam exhaust recovering device, it is characterized in that: described nozzle is threaded with suction chamber.
Above-mentioned injecting type low pressure steam exhaust recovering device is characterized in that: described low pressure exhaust steam entrance is connected with the top of suction chamber.
Above-mentioned injecting type low pressure steam exhaust recovering device is characterized in that: the connected mode of described suction chamber and mixing chamber is welding.
The utility model compared with prior art has the following advantages:
1, the utility model is simple in structure, reasonable in design and use easy and simple to handle.
2, the utility model will have the cold water of certain pressure by after the nozzle ejection, form low-pressure area at low pressure exhaust steam entrance location place, the low pressure exhaust steam will enter suction chamber and cold water mix heat exchange under swabbing action like this, and then the low pressure exhaust steam becomes condensate water and flows out recycling with the working water that has been heated through hot water outlet.Therefore, the utlity model has energy-saving and environmental protection, characteristics that economic worth is high.
3, the utility model friction, noiselessness, without corrosion, stable.
4, the utility model is lightweight, and floor space is little, can be in very narrow space mounting operation.
5, the utility model is safe and reliable, can well satisfy Production requirement, reaches the waste heat recovery purpose, has created huge economic benefit and social benefit.
6, the utility model has effectively utilized the low pressure exhaust steam, is the comprehensive saving to coal, oil, electricity, and water balance, the thermal balance of enterprise is had important intensive optimization function, and macro adjustments and controls and the sustainable development of whole national economy had good booster action; Owing to reduced the consumption of the energy, also just indirectly reduced to the chance of airborne release flue dust and sulfide simultaneously, greatly reduced exhaust noise, played environmental-protection function, economic benefit and social synthesis's benefit are very considerable.
7, the utility model scope of application is wide, and the low pressure exhaust steam with a large amount of heat energy that can effectively be applicable to emit in the industry production processes such as electric power, chemical industry, metallurgy, iron and steel is reclaimed, and plays energy-conserving and environment-protective, energy-saving and cost-reducing effect.
Below by drawings and Examples, the utility model is described in further detail.
Description of drawings
Fig. 1 is overall structure schematic diagram of the present utility model.
Description of reference numerals:
1-cold water inlet; 2-nozzle; 3-suction chamber;
4-low pressure exhaust steam entrance; 5-mixing chamber; 6-hot water outlet.
The specific embodiment
As shown in Figure 1, the utility model comprises suction chamber 3, mixing chamber 5, nozzle 2, low pressure exhaust steam entrance 4, cold water inlet 1 and hot water outlet 6; Described low pressure exhaust steam entrance 4 is connected with suction chamber 3, described nozzle 2 is arranged on the inside of suction chamber 3 and is connected with the arrival end of suction chamber 3, described cold water inlet 1 is connected with the arrival end of nozzle 2, the port of export of described suction chamber 3 is connected with the arrival end of mixing chamber 5, and the port of export of described mixing chamber 5 is connected with hot water outlet 6.
As shown in Figure 1, the port of export of described mixing chamber 5 is diffuser and is horn-like, and diffuser plays a part to slow down, boost to hot water, guarantees that hot water normally carries.
In the present embodiment, described nozzle 2 is threaded with suction chamber 3, can regulate as required like this distance between the arrival end of the port of export of nozzle 2 and mixing chamber 5, to guarantee result of use.
As shown in Figure 1, described low pressure exhaust steam entrance 4 is connected with the top of suction chamber 3.
In the present embodiment, described suction chamber 3 is welding with the connected mode of mixing chamber 5.
In conjunction with Fig. 1, operation principle of the present utility model is: the cold water with certain pressure enters nozzle 2 through cold water inlet 1, jet-action by nozzle 2, a part of pressure energy of cold water is converted into the speed energy, the pressure decreased of cold water, will form the low-pressure area (can reach negative pressure) that a pressure is lower than the low pressure exhaust steam relatively at suction chamber 3 places, the low pressure exhaust steam will enter mixing chamber 5 after low pressure exhaust steam entrance 4 is sucked into suction chamber 3 and the preliminary mixed heat transfer of cold water like this, in mixing chamber 5, cold water carries out sufficient energy exchange with the low pressure exhaust steam with a large amount of heat energy, low pressure exhaust steam cooling all becomes condensate water, cold water is heated simultaneously, cold water and low pressure exhaust steam enter diffuser again behind abundant mixed heat transfer in mixing chamber 5, flow rate of hot water reduces in diffuser, make the heat hydraulic pressure recover to guarantee normal conveying, last hot water flows out from hot water outlet 6, reaches normal delivering hot water for the user.
The above; it only is preferred embodiment of the present utility model; be not that the utility model is imposed any restrictions; every according to the utility model technical spirit to any simple modification, change and equivalent structure transformation that above embodiment does, all still belong in the protection domain of technical solutions of the utility model.

Claims (5)

1. an injecting type low pressure steam exhaust recovering device is characterized in that: comprise suction chamber (3), mixing chamber (5), nozzle (2), low pressure exhaust steam entrance (4), cold water inlet (1) and hot water outlet (6); Described low pressure exhaust steam entrance (4) is connected with suction chamber (3), described nozzle (2) is arranged on the inside of suction chamber (3) and is connected with the arrival end of suction chamber (3), described cold water inlet (1) is connected with the arrival end of nozzle (2), the port of export of described suction chamber (3) is connected with the arrival end of mixing chamber (5), and the port of export of described mixing chamber (5) is connected with hot water outlet (6).
2. according to injecting type low pressure steam exhaust recovering device claimed in claim 1, it is characterized in that: the port of export of described mixing chamber (5) is diffuser and is horn-like.
3. according to claim 1 or 2 described injecting type low pressure steam exhaust recovering devices, it is characterized in that: described nozzle (2) is threaded with suction chamber (3).
4. according to claim 1 or 2 described injecting type low pressure steam exhaust recovering devices, it is characterized in that: described low pressure exhaust steam entrance (4) is connected with the top of suction chamber (3).
5. according to claim 1 or 2 described injecting type low pressure steam exhaust recovering devices, it is characterized in that: described suction chamber (3) is welding with the connected mode of mixing chamber (5).
CN 201220337866 2012-07-13 2012-07-13 Jet type low-pressure waste steam recovery device Expired - Fee Related CN202719899U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220337866 CN202719899U (en) 2012-07-13 2012-07-13 Jet type low-pressure waste steam recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220337866 CN202719899U (en) 2012-07-13 2012-07-13 Jet type low-pressure waste steam recovery device

Publications (1)

Publication Number Publication Date
CN202719899U true CN202719899U (en) 2013-02-06

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CN (1) CN202719899U (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103727814A (en) * 2013-12-08 2014-04-16 无锡市优耐特石化装备有限公司 Concave fusiform exchanger for ejected fluid
CN104006679A (en) * 2014-05-23 2014-08-27 杨晓平 Multistage composite pressurized hot water generator
CN104534446A (en) * 2014-11-30 2015-04-22 贵阳铝镁设计研究院有限公司 Method and device for reducing energy losses of drain flash tank
CN104567463A (en) * 2013-10-23 2015-04-29 洛阳蓝海实业有限公司 Low-pressure vapor recovery unit
CN104692345A (en) * 2013-12-04 2015-06-10 山东联合化工股份有限公司 Equipment system for recovering exhaust steam of steam
CN108224402A (en) * 2018-03-06 2018-06-29 西安西热锅炉环保工程有限公司 Exhaust steam residual heat retracting device is arranged surely by a kind of thermal power plant
CN112357043A (en) * 2020-10-28 2021-02-12 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) Ship diesel power system
CN112357040A (en) * 2020-10-28 2021-02-12 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) Ship diesel power system
CN112357038A (en) * 2020-10-28 2021-02-12 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) Steam powered outboard conformal cooling system
CN112393625A (en) * 2020-11-19 2021-02-23 山东汉华工业设备有限公司 Evaporate cauldron exhaust steam and retrieve heat exchanger group
CN114151389A (en) * 2021-12-07 2022-03-08 宁波金发新材料有限公司 Low-pressure steam recycling device
US20220126969A1 (en) * 2020-10-28 2022-04-28 Wuhan Second Ship Design And Research Institute Marine Diesel Power System

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104567463A (en) * 2013-10-23 2015-04-29 洛阳蓝海实业有限公司 Low-pressure vapor recovery unit
CN104692345A (en) * 2013-12-04 2015-06-10 山东联合化工股份有限公司 Equipment system for recovering exhaust steam of steam
CN103727814A (en) * 2013-12-08 2014-04-16 无锡市优耐特石化装备有限公司 Concave fusiform exchanger for ejected fluid
CN104006679A (en) * 2014-05-23 2014-08-27 杨晓平 Multistage composite pressurized hot water generator
CN104006679B (en) * 2014-05-23 2016-01-13 杨晓平 Multistage composite pressurized hot water generator
CN104534446A (en) * 2014-11-30 2015-04-22 贵阳铝镁设计研究院有限公司 Method and device for reducing energy losses of drain flash tank
CN108224402A (en) * 2018-03-06 2018-06-29 西安西热锅炉环保工程有限公司 Exhaust steam residual heat retracting device is arranged surely by a kind of thermal power plant
CN112357040A (en) * 2020-10-28 2021-02-12 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) Ship diesel power system
CN112357043A (en) * 2020-10-28 2021-02-12 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) Ship diesel power system
CN112357038A (en) * 2020-10-28 2021-02-12 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) Steam powered outboard conformal cooling system
CN112357038B (en) * 2020-10-28 2021-11-09 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) Steam powered outboard conformal cooling system
US20220126969A1 (en) * 2020-10-28 2022-04-28 Wuhan Second Ship Design And Research Institute Marine Diesel Power System
WO2022088530A1 (en) * 2020-10-28 2022-05-05 武汉第二船舶设计研究所 Steam-powered outboard conformal cooling system
US11987337B2 (en) * 2020-10-28 2024-05-21 Wuhan Second Ship Design And Research Institute Marine diesel power system
CN112393625A (en) * 2020-11-19 2021-02-23 山东汉华工业设备有限公司 Evaporate cauldron exhaust steam and retrieve heat exchanger group
CN114151389A (en) * 2021-12-07 2022-03-08 宁波金发新材料有限公司 Low-pressure steam recycling device
CN114151389B (en) * 2021-12-07 2024-05-28 宁波金发新材料有限公司 Low-pressure steam recycling device

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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130206

Termination date: 20140713

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