CN204554782U - A kind of plant gas heat energy utilization system - Google Patents
A kind of plant gas heat energy utilization system Download PDFInfo
- Publication number
- CN204554782U CN204554782U CN201520222795.0U CN201520222795U CN204554782U CN 204554782 U CN204554782 U CN 204554782U CN 201520222795 U CN201520222795 U CN 201520222795U CN 204554782 U CN204554782 U CN 204554782U
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- China
- Prior art keywords
- oxygen
- eliminating device
- drain tank
- discharging door
- heater
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- Expired - Fee Related
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- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The utility model discloses a kind of plant gas heat energy utilization system, comprise oxygen-eliminating device a, oxygen-eliminating device b, heater and drain tank, described oxygen-eliminating device a, the connector of oxygen-eliminating device b by placed in series together, the oxygen exhaust of described oxygen-eliminating device a and oxygen-eliminating device b is equipped with an oxygen discharging door and secondary oxygen discharging door, described heater is connected with between a described oxygen discharging door and secondary oxygen discharging door, an inlet valve is provided with in the side of described heater, described inlet valve is connected with described drain tank by booster pump a, also be connected on described drain tank at the opposite side of described heater.There is a large amount of waste heat in the waste gas produced in the utility model industrial production and obtain effective utilization, thus make enterprise obtain the low waste gas afterheat recovery unit of cost, for Reducing Cost in Enterprises, increase wound benefit, really realize energy-saving and emission-reduction.
Description
Technical field
The utility model relates to the field of Environment Protection in coal power station, is specially a kind of plant gas heat energy utilization system.
Background technology
At present, in each factory, waste gas residual heat overbottom pressure is utilized to be the Important Action that industry energy conservation reduces discharging, also
It is a vital task of country! As when existing two oxygen-eliminating devices in steam turbine post in some in factory, every platform oxygen-eliminating device exert oneself as 100t/h, oxygen-eliminating device operating pressure is 0.49MPa, and temperature is 150
0c, in order to supply the qualified stove water of oxygen content to boiler, just must the water pressurization 1.0MPa in oxygen-eliminating device, simultaneous temperature adds to 200
0c, makes the oxygen in oxygen-eliminating device in water separate from water; In order to reach good deaerating effect, need a certain amount of steam with oxygen discharged to air.General Electric Power Design Institute when designing, due to oxygen and steam segregation ratio more difficult, complex process and cost is high, so will not reclaim the deoxygenation steam of oxygen-eliminating device, this part steam can not be utilized effectively, and energy waste is very serious.
Utility model content
The technical problem that the utility model solves is to provide a kind of plant gas heat energy utilization system, to solve the shortcoming in above-mentioned background technology.
The technical problem that the utility model solves realizes by the following technical solutions: a kind of plant gas heat energy utilization system, comprise the oxygen-eliminating device a for removing oxygen and oxygen-eliminating device b, the heater utilizing waste heat to carry out heating and drain tank, the connector of described oxygen-eliminating device a, oxygen-eliminating device b by placed in series together, the oxygen exhaust of described oxygen-eliminating device a and oxygen-eliminating device b is equipped with an oxygen discharging door and secondary oxygen discharging door, be provided with triple valve between an oxygen discharging door on described oxygen-eliminating device a and oxygen-eliminating device b, secondary oxygen discharging door, between two triple valves, pass through tubes connection.Described heater is connected with between a described oxygen discharging door and secondary oxygen discharging door, an inlet valve is provided with in the side of described heater, described inlet valve is connected with described drain tank by booster pump a, also be connected on described drain tank at the opposite side of described heater, the pipeline on the connector of described oxygen-eliminating device a and oxygen-eliminating device b is connected on described drain tank by booster pump b.
In the utility model, described booster pump a and booster pump b is equipped with several valves, described valve is two inlet valves and a flowing water Valve respectively.
The beneficial effects of the utility model: there is a large amount of waste heat in the waste gas produced in industrial production and obtain effective utilization, thus make enterprise obtain the low waste gas afterheat recovery unit of cost, for Reducing Cost in Enterprises, increase wound benefit, really realize energy-saving and emission-reduction.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
In figure: 1-oxygen-eliminating device a, 2-oxygen-eliminating device b, 3-heater, 4-drain tank, 5-oxygen discharging door, 6-bis-oxygen discharging doors, 7-inlet valve, 8-booster pump a, 9-booster pump b.
Detailed description of the invention
The technological means realized to make the utility model, creation characteristic, reaching object and effect is easy to understand, below in conjunction with concrete diagram, setting forth the utility model further.
As shown in Figure 1, a kind of plant gas heat energy utilization system, comprise oxygen-eliminating device a1, oxygen-eliminating device b2, heater 3 and drain tank 4, described oxygen-eliminating device a1, the connector of oxygen-eliminating device b2 by placed in series together, the oxygen exhaust of described oxygen-eliminating device a1 and oxygen-eliminating device b2 is equipped with an oxygen discharging door 5 and secondary oxygen discharging door 6, described heater 3 is connected with between a described oxygen discharging door 5 and secondary oxygen discharging door 6, an inlet valve 7 is provided with in the side of described heater 3, described inlet valve 7 is connected with described drain tank 4 by booster pump a8, also be connected on described drain tank 4 at the opposite side of described heater 3.
In the utility model, be provided with triple valve between an oxygen discharging door 5 on described oxygen-eliminating device a1 and oxygen-eliminating device b2, secondary oxygen discharging door 6, between two triple valves, pass through tubes connection.
In the utility model, the pipeline on the connector of described oxygen-eliminating device a1 and oxygen-eliminating device b2 is connected on described drain tank 4 by booster pump b9.
In the utility model, described booster pump a8 and booster pump b9 is equipped with several valves.
In the utility model, described valve is two inlet valves and a flowing water Valve respectively.
Oxygen-eliminating device waste heat hydraulic recovery adopts the heater 3 one of FYW-80 type injecting type mixing.Utilize existing drain tank 4, a part of water is extracted out from drain tank 4, the booster pump a8 newly installed additional is utilized to pressurize, fluidic vectoring thrust negative pressure is produced in contact(-type) heater, the steam that oxygen-eliminating device is discharged is sucked back in heater 3, makes this part exhaust steam all be condensed into condensate water with water mixed heat transfer, return drain tank 4 together with the water that drain tank is extracted out, hydrophobic in heating drain tank 4, the steam drain that the oxygen reclaimed from oxygen-eliminating device is then newly installed additional by drain tank 4 is discharged to air.
For heating the hydrophobic of drain tank 4 after the steam discharge of oxygen-eliminating device a1, oxygen-eliminating device b2 all reclaims, from 24 of drain tank 4
0the hydrophobic of about C is heated to 92 through exhaust steam heater
0c, then enter in drain tank 4 water temperature in drain tank 4 is increased to 51
0c.Like this, the water temperature of drain tank 4 is by original 24
0c is increased to 51
0c, the water temperature entirety of drain tank 4 improves 27
0c squeezes into the water of drain tank in oxygen-eliminating device and heats, and when not installing oxygen-eliminating device waste heat residual pressure recovering equipment additional, drain tank 4 enters the drain temperature of oxygen-eliminating device 24
0about C.
After oxygen-eliminating device waste heat residual pressure recovering equipment is installed, can water temperature 24
0c's is hydrophobic through contact(-type) heater, by 104
0the steam of C makes drain temperature be increased to 92
0c, then enter in drain tank through piping, to make in drain tank 4 water temp. heating to 51
0c.Because this system is continuously run, as long as the throttle (steam) temperature of contact(-type) heater remains unchanged, the drain temperature so in drain tank 4 also remains on 51 always
0c.To put into operation situation from this device, this device can meet need of production, and the waste heat overbottom pressure that oxygen-eliminating device is discharged is fully used again, hydrophobic by 24 in drain tank
0c is increased to 51
0c, entirety improves 27
0c.Both ensured the recycling of oxygen-eliminating device exhaust steam, also ensure that the separation discharge of oxygen discharged by oxygen-eliminating device.
More than show and describe general principle of the present utility model and principal character and advantage of the present utility model, the technical staff of the industry should understand, the utility model is not restricted to the described embodiments, what describe in above-described embodiment and description just illustrates principle of the present utility model, under the prerequisite not departing from the utility model spirit and scope, the utility model also has various changes and modifications, these changes and improvements all fall within the scope of claimed the utility model, the claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (5)
1. a plant gas heat energy utilization system, comprise oxygen-eliminating device a(1), oxygen-eliminating device b(2), heater (3) and drain tank (4), it is characterized in that: described oxygen-eliminating device a(1), oxygen-eliminating device b(2) connector by placed in series together, at described oxygen-eliminating device a(1) and oxygen-eliminating device b(2) oxygen exhaust on be equipped with an oxygen discharging door (5) and secondary oxygen discharging door (6), described heater (3) is connected with between a described oxygen discharging door (5) and secondary oxygen discharging door (6), an inlet valve (7) is provided with in the side of described heater (3), described inlet valve (7) is by booster pump a(8) be connected with described drain tank (4), also be connected on described drain tank (4) at the opposite side of described heater (3).
2. a kind of plant gas heat energy utilization system according to claim 1, it is characterized in that: described oxygen-eliminating device a(1) and oxygen-eliminating device b(2) on an oxygen discharging door (5), secondary oxygen discharging door be provided with triple valve between (6), pass through tubes connection between two triple valves.
3. a kind of plant gas heat energy utilization system according to claim 1, is characterized in that: described oxygen-eliminating device a(1) and oxygen-eliminating device b(2) connector on pipeline by booster pump b(9) be connected on described drain tank (4).
4. a kind of plant gas heat energy utilization system according to claim 1, is characterized in that: described booster pump a(8) and booster pump b(9) on be equipped with several valves.
5. a kind of plant gas heat energy utilization system according to claim 4, is characterized in that: described valve is two inlet valves and a flowing water Valve respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520222795.0U CN204554782U (en) | 2015-04-15 | 2015-04-15 | A kind of plant gas heat energy utilization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520222795.0U CN204554782U (en) | 2015-04-15 | 2015-04-15 | A kind of plant gas heat energy utilization system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204554782U true CN204554782U (en) | 2015-08-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520222795.0U Expired - Fee Related CN204554782U (en) | 2015-04-15 | 2015-04-15 | A kind of plant gas heat energy utilization system |
Country Status (1)
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| CN (1) | CN204554782U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106439783A (en) * | 2016-10-17 | 2017-02-22 | 北京京诚科林环保科技有限公司 | Heat energy efficient utilization system capable of heating fan heater while recycling dead steam of deoxygenization plant |
| CN106949455A (en) * | 2017-03-23 | 2017-07-14 | 东莞市金田纸业有限公司 | A kind of noise-reduction energy-saving device applied to oxygen-eliminating device |
-
2015
- 2015-04-15 CN CN201520222795.0U patent/CN204554782U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106439783A (en) * | 2016-10-17 | 2017-02-22 | 北京京诚科林环保科技有限公司 | Heat energy efficient utilization system capable of heating fan heater while recycling dead steam of deoxygenization plant |
| CN106949455A (en) * | 2017-03-23 | 2017-07-14 | 东莞市金田纸业有限公司 | A kind of noise-reduction energy-saving device applied to oxygen-eliminating device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150812 Termination date: 20160415 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |