CN201680356U - Condensed water energy recovery device - Google Patents
Condensed water energy recovery device Download PDFInfo
- Publication number
- CN201680356U CN201680356U CN2010201507398U CN201020150739U CN201680356U CN 201680356 U CN201680356 U CN 201680356U CN 2010201507398 U CN2010201507398 U CN 2010201507398U CN 201020150739 U CN201020150739 U CN 201020150739U CN 201680356 U CN201680356 U CN 201680356U
- Authority
- CN
- China
- Prior art keywords
- water
- energy
- condensed water
- absorbing district
- condensed
- 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
Links
Images
Landscapes
- Management, Administration, Business Operations System, And Electronic Commerce (AREA)
Abstract
The embodiment of the utility model discloses a condensed water energy recovery device, which comprises a heat insulation water storage tank, a flow blocking device, a water distributor and a softening water inlet pipe, an exhaust pipe and a water pump, wherein the flow blocking device is arranged in the heat insulation water storage tank and divides the heat insulation water tank into a mixed energy absorbing region and a constant-temperature energy absorbing region, the top part of the heat insulation water storage tank is provided with a softening water pipeline, a condensed water inlet is arranged in the mixed energy absorbing region of the heat insulation water storage tank, the water distributor and the softening water inlet pipe are connected with the softening water pipeline in a flow dividing way, and are arranged in the heat insulation energy absorbing region, the water distributor is arranged on the top part of the heat insulation water storage tank and the mixed energy absorbing region, the exhaust pipe is arranged on the top part of the constant-temperature energy absorbing region of the heat insulation water storage tank, and the water pump is connected with an outlet of the constant-temperature energy absorbing region of the heat insulation water storage tank. The condensed water energy recovery device provided by the utility model recovers the energy in the condensed water, and improves the recovery rate of energy in the condensed water.
Description
Technical field
The utility model relates to condensed water apparatus for energy recovery manufacturing technology field, more particularly, relates to a kind of condensed water energy recycle device.
Background technology
At present, energy shortage, global warming, low-carbon economy is all being carried out in the whole world, and now domestic each enterprise energy waste is serious, particularly the low energy that causes of reclamation of condensate water utilization rate runs off very serious.Existing a kind of open type condensation water recovery system, its condensed water removal process is as shown in Figure 1: the condensed water that steam forms after the process equipment heat exchange is drained into it in collecting tank that drain valve pump is installed by drain valve, rely on condensate pump that condensed water is transported to the boiler room then, the shortcoming of existing open type condensation water recovery system is: high temperature, step-down suddenly produced a large amount of flash steams after the condensed water of high pressure arrived collecting tank, contain a large amount of heats in the flash steam, and with collect that tank connected gland steam exhauster is inevasible in the process of discharging waste gas to have discharged a large amount of flash steams, flash steam just is discharged like this, causes the waste of energy.
The utility model content
In view of this, the utility model provides a kind of condensed water energy recycle device, reclaims the energy dissipation problem that causes in the condensed water process to solve existing condensation water recovery system.
For achieving the above object, the utility model provides following technical scheme:
A kind of condensed water energy recycle device comprises:
The insulation water tank;
Be arranged on the choke apparatus that in the described insulation water tank described insulation water tank is divided into mixing energy-absorbing district and constant temperature energy-absorbing district, the top of described insulation water tank is provided with the demineralized water pipeline, and the mixing energy-absorbing district of described insulation water tank is provided with the condensed water import;
Shunt water-distributing device and the demineralized water water inlet pipe that is connected and is arranged on described insulation energy-absorbing district with described demineralized water pipeline, described water-distributing device is arranged on the top in the mixing energy-absorbing district of described insulation water tank;
Be arranged on the blast pipe at the top, constant temperature energy-absorbing district of described insulation water tank;
The water pump that is connected with the outlet in the constant temperature energy-absorbing district of described insulation water tank.
Preferably, in the above-mentioned condensed water energy recycle device, also comprise the secondary moisture film heat sink that is arranged on the described blast pipe, the water inlet of described secondary moisture film heat sink is connected with described demineralized water pipeline.
Preferably, in the above-mentioned condensed water energy recycle device, also comprise the mixing energy-absorbing district and the corresponding condensate water guide device of described condensed water import that are arranged on described heat preservation storage water tank, the export mouth of described condensate water guide device is equal with the mouth of pipe of described demineralized water water inlet pipe.
Preferably, in the above-mentioned condensed water energy recycle device, described water pump is an electric water pump.
Preferably, in the above-mentioned condensed water energy recycle device, also comprise the temperature controller of controlling demineralized water flow in the described demineralized water pipeline according to the temperature in described constant temperature energy-absorbing district.
From above-mentioned technical scheme as can be seen, in the condensed water energy recycle device that is provided among the utility model embodiment, be arranged on the water-distributing device that mixes the energy-absorbing district and make demineralized water and high temperature, the condensed water of high pressure is collected step-down suddenly produces behind the insulation water tank flash steam and is fully contacted mixing the energy-absorbing district, demineralized water absorbs the energy of flash steam rapidly, and condensed water enters the demineralized water that mixes behind the energy-absorbing district with in the demineralized water water pipe and mixes, energy in the condensed water is absorbed, mixed water further fully mixes in constant temperature energy-absorbing district by forming drop behind the choke apparatus, make the energy in the condensed water absorb more fully, form the identical mixing water of water temperature everywhere, the water pump that is connected with the outlet in constant temperature energy-absorbing district is recovered to mixing water in the boiler room softening water tank, realize recycling, condensate water recovery device in the utility model is by the energy in the flash steam of demineralized water absorption condensation water and condensed water generation, realize the recycling of energy in the condensed water, improved the organic efficiency of energy.
Description of drawings
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, to do to introduce simply to the accompanying drawing of required use in embodiment or the description of the Prior Art below, apparently, accompanying drawing in describing below only is embodiment more of the present utility model, for those of ordinary skills, under the prerequisite of not paying creative work, can also obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is existing open type condensation water recovery system technological principle schematic diagram;
The condensed water energy recycle device structural representation that Fig. 2 provides for the utility model embodiment.
The specific embodiment
For quote and know for the purpose of, below the drawing reference numeral in the accompanying drawing is explained as follows:
1, insulation water tank, 2, the condensate water guide device, 3, water-distributing device, 4, choke apparatus, 5, secondary moisture film heat sink, 6, electric water pump, 7, the demineralized water water inlet pipe, A, mix the energy-absorbing district, B, constant temperature energy-absorbing district, C, condensed water import, D, demineralized water pipeline.
Below in conjunction with the accompanying drawing among the utility model embodiment, the technical scheme among the utility model embodiment is clearly and completely described, obviously, described embodiment only is the utility model part embodiment, rather than whole embodiment.Based on the embodiment in the utility model, those of ordinary skills are not making the every other embodiment that is obtained under the creative work prerequisite, all belong to the scope of the utility model protection.
The utility model embodiment discloses a kind of condensed water energy recycle device, to improve the recycling to energy in the condensed water.
As shown in Figure 2, a kind of condensed water energy recycle device comprises: insulation water tank 1, condensate water guide device 2, water-distributing device 3, choke apparatus 4, secondary moisture film heat sink 5, electric water pump 6 and demineralized water water inlet pipe 7, wherein:
Be provided with choke apparatus 4 in the insulation water tank 1, choke apparatus 4 will be incubated water tank 1 and be divided into mixing energy-absorbing district A and constant temperature energy-absorbing district B;
The top of insulation water tank 1 is provided with demineralized water pipeline D, and the end of the mixing energy-absorbing district A of insulation water tank is provided with the condensed water import, and arrow is the flow direction of water in the accompanying drawing 2;
Be connected with water-distributing device 3 and demineralized water water inlet pipe 7 with described demineralized water pipeline D shunting;
The top of the constant temperature energy-absorbing district B of insulation water tank 1 is provided with blast pipe, and secondary moisture film heat sink 5 is installed on the blast pipe, and the water inlet of secondary moisture film heat sink 5 is connected with the demineralized water pipeline; The outlet of the constant temperature energy-absorbing district B of insulation water tank 1 is connected with electric water pump 6, between the outlet of electric water pump 6 and constant temperature energy-absorbing district B switch valve is installed.
The mixing energy-absorbing district A of heat preservation storage water tank 1 also is provided with the corresponding condensate water guide device 2 with described condensed water import C, and the export mouth of condensate water guide device 2 is equal with the mouth of pipe of described demineralized water water pipe 7.
The course of work of condensate water recovery device provided by the utility model is as follows: condensed water flows into the insulation water tank 1 from the condensed water import C of insulation water tank, high temperature, when the condensed water of high pressure flows to insulation water tank 1 from condensing water conduit, because the unexpected reduction of pressure, condensed water will produce flash steam after flowing into insulation water tank 1, the water-distributing device 3 that be incubated the top of the mixing energy-absorbing district A in the water tank 1 this moment makes demineralized water fully mix with flash steam, absorb the heat in the flash steam, waste gas in the final condensed water is discharged through blast pipe, condensation flow is mixed with the demineralized water of demineralized water water inlet pipe 7 outflows after mixing energy-absorbing district A in addition, energy in the demineralized water absorption condensation water in the demineralized water water pipe 7, mixing water forms drop through choke apparatus 4 fully to be mixed once more at constant temperature energy-absorbing district B, reaches the purpose that energy in the condensed water is fully absorbed.Last mixing water is transported in the boiler room softening water tank through electric water pump 6 through the outlet of constant temperature energy-absorbing district B, condensed water energy recycle device in the utility model mixes back absorption heat wherein by demineralized water with the flash steam of condensed water and generation thereof, and mixing water is recovered in the boiler room softening water tank reuses, improve the recycling of energy in the condensed water, reduced the waste of energy.
Secondary moisture film heat sink 5 is installed on the blast pipe in the foregoing description, the water inlet of the heat sink 5 of secondary moisture film is connected with demineralized water pipeline D, when the waste gas in the insulation water tank 1 is discharged, carry out heat exchange with the moisture in the secondary moisture film heat sink 5, make the heat in the condensed water further obtain reclaiming, guarantee the eliminating of no flash steam fully, improved the organic efficiency of energy in the condensed water.
The corresponding position of condensed water import C in the foregoing description in the mixing energy-absorbing district A of heat preservation storage water tank 1 is provided with condensate water guide device 2, the export mouth of condensate water guide device 2 is corresponding with the mouth of pipe of demineralized water water pipe 7, condensed water is flowed out by flow-guiding mouth through condensate water guide device 4 backs, and the mouth of pipe of demineralized water water pipe 7 is corresponding with flow-guiding mouth, demineralized water can mix in the very first time more fully fast with condensed water, reaches the purpose of energy absorption.
Also can be provided with temperature controller in constant temperature energy-absorbing district B in the foregoing description, temperature controller can be controlled the demineralized water flow of described demineralized water import according to the temperature of constant temperature energy-absorbing district B.
The condensed water energy recycle device that is provided in the foregoing description has reclaimed the energy in the condensed water fully, has improved energy recovery efficiency, has guaranteed the discharge of no flash steam, has reduced noise and thermal pollution.
What adopt in the condensed water energy recycle device that is provided in the foregoing description is electric water pump, and existing open type condensation water recovery system adopts is the drain valve pump, and the drain valve pump scope of application is little, needs steam drive, need corresponding steam pipework and steam valve accessory, electric water pump in the utility model is ordered about by electricity, and usage range is wide, need not steam drive, need not corresponding steam pipework and steam valve accessory, simple in structure, maintenance rate is low, and is easy to maintenance.
In the condensed water energy recycle device that is provided among the utility model embodiment; on the pipeline that the outlet in condensed water water inlet, demineralized water water inlet and constant temperature energy-absorbing district is connected, all be provided with various control valves; so that the fluid in the pipe is better controlled; no matter in addition which type of application valve body can not influence the protection domain of the condensed water energy recycle device that the utility model embodiment provided.
Each embodiment adopts the mode of going forward one by one to describe in this specification, and what each embodiment stressed all is and the difference of other embodiment that identical similar part is mutually referring to getting final product between each embodiment.
To the above-mentioned explanation of the disclosed embodiments, make this area professional and technical personnel can realize or use the utility model.Multiple modification to these embodiment will be conspicuous concerning those skilled in the art, and defined herein General Principle can realize under the situation that does not break away from spirit or scope of the present utility model in other embodiments.Therefore, the utility model will can not be restricted to these embodiment shown in this article, but will meet and principle disclosed herein and features of novelty the wideest corresponding to scope.
Claims (5)
1. a condensed water energy recycle device is characterized in that, comprising:
The insulation water tank;
Be arranged on the choke apparatus that in the described insulation water tank described insulation water tank is divided into mixing energy-absorbing district and constant temperature energy-absorbing district, described insulation water tank top is provided with the demineralized water pipeline, and the mixing energy-absorbing district of described insulation water tank is provided with the condensed water import;
Shunt water-distributing device and the demineralized water water inlet pipe that is connected and is arranged on described insulation energy-absorbing district with described demineralized water pipeline, described water-distributing device is arranged on the top in the mixing energy-absorbing district of described insulation water tank;
Be arranged on the blast pipe at the top, constant temperature energy-absorbing district of described insulation water tank;
The water pump that is connected with the outlet in the constant temperature energy-absorbing district of described insulation water tank.
2. condensed water energy recycle device according to claim 1 is characterized in that, also comprises the secondary moisture film heat sink that is arranged on the described blast pipe, and the water inlet of described secondary moisture film heat sink is connected with the pipeline of described demineralized water import.
3. condensed water energy recycle device according to claim 1 and 2, it is characterized in that, also comprise the mixing energy-absorbing district and the corresponding condensate water guide device of described condensed water import that are arranged on described heat preservation storage water tank, the export mouth of described condensate water guide device is equal with the mouth of pipe of described demineralized water water pipe.
4. condensed water energy recycle device according to claim 3 is characterized in that, described water pump is an electric water pump.
5. condensate water recovery device according to claim 4 is characterized in that, also comprises temperature controller, and described temperature controller is controlled the flow of described demineralized water import according to the temperature in described constant temperature energy-absorbing district.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201507398U CN201680356U (en) | 2010-03-30 | 2010-03-30 | Condensed water energy recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201507398U CN201680356U (en) | 2010-03-30 | 2010-03-30 | Condensed water energy recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201680356U true CN201680356U (en) | 2010-12-22 |
Family
ID=43345399
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201507398U Expired - Fee Related CN201680356U (en) | 2010-03-30 | 2010-03-30 | Condensed water energy recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201680356U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107421377A (en) * | 2017-07-28 | 2017-12-01 | 河南中烟工业有限责任公司 | A kind of heat exchanger condensed water open type steam trap connection and its application method |
-
2010
- 2010-03-30 CN CN2010201507398U patent/CN201680356U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107421377A (en) * | 2017-07-28 | 2017-12-01 | 河南中烟工业有限责任公司 | A kind of heat exchanger condensed water open type steam trap connection and its application method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204006255U (en) | A kind of waste heat recovery central heating system | |
| CN103604244B (en) | Multi-resource low-temperature waste heat comprehensive utilization system | |
| CN203757824U (en) | Heat supply system capable of reducing return water temperature of primary network | |
| CN207050270U (en) | A kind of sulfur removal technology residual neat recovering system | |
| CN203203020U (en) | Steam waste heat water recycling device for machining paper | |
| CN105993722A (en) | Solar heating warming system for vegetable fruit greenhouse | |
| CN201680356U (en) | Condensed water energy recovery device | |
| CN101368749B (en) | Recirculated water low-level regenerated energy heating system of cooling column in thermal plant and refrigeration plant | |
| CN111378796A (en) | Equipment system and process principle of waste heat utilization of converter steel slag | |
| CN102435015A (en) | Condensation heat recovery device in power station | |
| CN204910833U (en) | Gasification oxygen -eliminating device steam heat reclaim unit | |
| CN205036418U (en) | Industry waste heat recovery of cogeneration of heat and power utilizes system | |
| CN204174154U (en) | Environment-friendly coke-quenching apparatus steam heat recovery tower | |
| CN202101308U (en) | Automatic recycling system for waste heat of heat supply | |
| CN201875687U (en) | Heat supply system for factory boiler | |
| CN201901653U (en) | Pipeline washing device of a dry-process acetylene generator | |
| CN204154008U (en) | A kind of fermentation tank sterilization waste hot steam heat reclamation device | |
| CN104032054A (en) | Triple co-supply system for utilization of waste heat of blast furnace bottom-filtration-method slag flushing water | |
| CN204779646U (en) | Novel two -period form converter coal gas waste heat recovery system | |
| CN203820804U (en) | System for preheating boiler water by washing blast furnace slag water | |
| CN204301024U (en) | A kind of rectifying column air cooling device heat-recovering generating plant | |
| CN208234842U (en) | A kind of wet process coke pressure quenching energy source recovery apparatus | |
| CN201215452Y (en) | Heat energy recovery device for sewage water of machinery platform | |
| CN200979288Y (en) | Waste water residual heat recovering device | |
| CN205756032U (en) | Vegetables and fruits booth solar heating temperature-increasing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20160923 Granted publication date: 20101222 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| PD01 | Discharge of preservation of patent | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20170323 Granted publication date: 20101222 |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101222 Termination date: 20160330 |