CN204534540U - For the raw water heater steam drainage recovery device of boiler feed water system - Google Patents
For the raw water heater steam drainage recovery device of boiler feed water system Download PDFInfo
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- CN204534540U CN204534540U CN201520174791.XU CN201520174791U CN204534540U CN 204534540 U CN204534540 U CN 204534540U CN 201520174791 U CN201520174791 U CN 201520174791U CN 204534540 U CN204534540 U CN 204534540U
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- water tank
- steam drainage
- outlet pipe
- drainage outlet
- pro desalting
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
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Abstract
The utility model relates to the raw water heater steam drainage recovery device for boiler feed water system, compared with prior art solves the defect that steam drainage recovery utilization rate is low.Steam drainage outlet pipe of the present utility model is provided with drain valve and electric conductive meter, steam drainage outlet pipe access pro desalting water tank, steam drainage outlet pipe is connected to bypass duct and bypass duct between pro desalting water tank and hydrophobic dirt-removing pipe, bypass duct access ultrafiltration water tank, pro desalting water tank is connected to chemical deionization system pipeline, ultrafiltration water tank is connected to counter-infiltration system pipeline, steam drainage outlet pipe is positioned at pro desalting water tank import department and pneumatic diaphragm valve A and check-valves A is installed, bypass duct is positioned at ultrafiltration water tank import department and pneumatic diaphragm valve B and check-valves B is installed.The steam drainage of raw water heater is recycled to the reuse of pro desalting water tank by the utility model, reduces the water withdrawal of boiler feed water system fresh water, and decreases the discharge capacity of waste water.
Description
Technical field
The utility model relates to boiler feed water system technical field, specifically for the raw water heater steam drainage recovery device of boiler feed water system.
Background technology
At present in power plant runs, boiler feed water system many employings ultrafiltration+counter-infiltration+ion-exchange demineralization technique.In winter, season in spring two (particularly the power plant of north cold area), for ensureing the normal operation of pro desalting system, raw water heater being set usually the former water of boiler feedwater is heated up, namely utilizing the steam in power plant to carry out former water heating.But in actual motion, adopt is reclaimed to the steam drainage of raw water heater more and drains into wastewater disposal basin by gutter.In fact, the steam drainage of raw water heater derives from the condensate water in power plant, and water quality is better, directly drains into wastewater disposal basin, causes the waste of water; Also the engineering had is using the water inlet of steam drainage as counter-infiltration system, but according to the ruuning situation of existing counter-infiltration system, steam drainage still can lose 25% " reverse osmosis concentrated water " after entering counter-infiltration system, and the optimization that cannot reach steam drainage is recycled.How to develop a kind of technical problem having become urgent need solution for boiler feed water system raw water heater steam drainage recovery device.
Utility model content
The purpose of this utility model is to solve the defect that in prior art, steam drainage recovery utilization rate is low, provides a kind of raw water heater steam drainage recovery device for boiler feed water system to solve the problems referred to above.
To achieve these goals, the technical solution of the utility model is as follows:
For the raw water heater steam drainage recovery device of boiler feed water system, comprise main building jet chimney, main building jet chimney access raw water heater, raw water heater picks out steam drainage outlet pipe, steam drainage outlet pipe is connected to hydrophobic dirt-removing pipe, hydrophobic dirt-removing pipe is provided with manual diaphragm valve, and hydrophobic dirt-removing pipe access hyperfiltration reverse-rinsing reclaims pond
Described steam drainage outlet pipe is provided with drain valve and electric conductive meter, steam drainage outlet pipe access pro desalting water tank, steam drainage outlet pipe is connected to bypass duct and bypass duct between pro desalting water tank and hydrophobic dirt-removing pipe, bypass duct access ultrafiltration water tank, pro desalting water tank is connected to chemical deionization system pipeline, ultrafiltration water tank is connected to counter-infiltration system pipeline, steam drainage outlet pipe is positioned at pro desalting water tank import department and pneumatic diaphragm valve A and check-valves A is installed, bypass duct is positioned at ultrafiltration water tank import department and pneumatic diaphragm valve B and check-valves B is installed.
Described steam drainage outlet pipe is provided with heat indicator and heat indicator between drain valve and electric conductive meter, the data output end of heat indicator is connected with the data input pin of electric conductive meter.
The pipeline absolute altitude of described steam drainage outlet pipe between drain valve and pro desalting water tank is higher than the height of pro desalting water tank.
beneficial effect
Raw water heater steam drainage recovery device for boiler feed water system of the present utility model, compared with prior art the steam drainage of raw water heater is recycled to the reuse of pro desalting water tank, reduce the water withdrawal of boiler feed water system fresh water, and decrease the discharge capacity of waste water, reach water saving, energy-conservation object.Decrease the consumption of the fresh water of boiler feed water system on the one hand, reduce the wastewater flow rate in hyperfiltration reverse-rinsing recovery pond on the other hand, reduce energy consumption.The utility model does not newly increase treatment facility, has designed by means of only electric conductive meter, pipeline and valve combination, and its structure is simple, cost investment is little, result of use is remarkable, suitable for large-scale promotion and application.
Accompanying drawing explanation
Fig. 1 is theory structure schematic diagram of the present utility model;
Fig. 2 is Construction Arrangement front view of the present utility model;
Wherein, 1-raw water heater, 2-pro desalting water tank, 3-ultrafiltration water tank, 4-hyperfiltration reverse-rinsing reclaim pond, 5-steam drainage outlet pipe, 6-hydrophobic dirt-removing pipe, 7-bypass duct, 8-drain valve, 9-pneumatic diaphragm valve A, 10-pneumatic diaphragm valve B, 11-manual diaphragm valve, 12-check-valves A, 13-check-valves B, 14-heat indicator, 15-electric conductive meter, 16-main building jet chimney, 17-chemical deionization system pipeline, 18-counter-infiltration system pipeline, 19-pneumatic stopping valve, 20-steam control valve, 21-check-valves C.
Detailed description of the invention
For making to have a better understanding and awareness architectural feature of the present utility model and effect of reaching, coordinating detailed description in order to preferred embodiment and accompanying drawing, being described as follows:
As shown in Figure 1, the raw water heater steam drainage recovery device for boiler feed water system described in the utility model, comprises main building jet chimney 16.Main building jet chimney 16 accesses raw water heater 1, and between main building jet chimney 16 and raw water heater 1, be provided with pneumatic stopping valve 19, steam control valve 20 and check-valves C21.Raw water heater 1 picks out steam drainage outlet pipe 5, steam drainage outlet pipe 5 is connected to hydrophobic dirt-removing pipe 6, and hydrophobic dirt-removing pipe 6 accesses hyperfiltration reverse-rinsing and reclaims pond 4.It is outdoor hypogee that hyperfiltration reverse-rinsing reclaims pond 4, processes for collecting sewage and delivering to boiler feedwater Raw water treatment system by waste water pump.Hydrophobic dirt-removing pipe 6 being provided with manual diaphragm valve 11, for controlling, the underproof hydrophobic hyperfiltration reverse-rinsing that drains into being reclaimed pond 4.
Steam drainage outlet pipe 5 is provided with drain valve 8 and electric conductive meter 15, drain valve 8 is for controlling steam drainage outlet pipe 5, and electric conductive meter 15 is for detecting the change of hydrophobic electrical conductivity in steam drainage outlet pipe 5.Steam drainage outlet pipe 5 accesses pro desalting water tank 2, pro desalting water tank 2 is connected to chemical deionization system pipeline 17, the water of pro desalting water tank 2 enters chemical deionization system and uses.Steam drainage outlet pipe 5 use threeway be connected to bypass duct 7, bypass duct 7 is between pro desalting water tank 2 and hydrophobic dirt-removing pipe 6, bypass duct 7 accesses ultrafiltration water tank 3, ultrafiltration water tank 3 is connected to counter-infiltration system pipeline 18, and the water of ultrafiltration water tank 3 enters counter-infiltration system and uses.Steam drainage outlet pipe 5 is positioned at pro desalting water tank 2 import department and pneumatic diaphragm valve A9 and check-valves A12 is installed, whether pneumatic diaphragm valve A9 enters pro desalting water tank for control in steam drainage outlet pipe 5 hydrophobic, and check-valves A12 can not pour in down a chimney for the water controlled in pro desalting water tank 2 and enters in steam drainage outlet pipe 5.Bypass duct 7 is positioned at ultrafiltration water tank 3 import department and is provided with pneumatic diaphragm valve B10 and check-valves B13, pneumatic diaphragm valve B10 is identical with check-valves A12 with pneumatic diaphragm valve A9 with the effect of check-valves B13.
Steam drainage outlet pipe 5 is provided with heat indicator 14, heat indicator 14 is between drain valve 8 and electric conductive meter 15, and the data output end of heat indicator 14 is connected with the data input pin of electric conductive meter 15.Electric conductive meter 15 has temperature compensation function, electric conductive meter 15 for detecting the change of hydrophobic middle electrical conductivity, and according to the detection signal of heat indicator 14, the electrical conductivity signal under adopting temperature compensation function automatically to export reference temperature.Pro desalting water tank 2 and ultrafiltration water tank 3 are outdoor arrangement and are highly about about 6m, because hydrophobic pressure is less, as shown in Figure 2, the pipeline absolute altitude of steam drainage outlet pipe 5 between drain valve 8 and pro desalting water tank 2, higher than the height of pro desalting water tank 2, ensures that the hydrophobic acquisition sufficiently high pressure of steam after raw water heater 1 heat exchange can enter pro desalting water tank 2.In like manner, the pipeline absolute altitude of steam drainage outlet pipe 5 between drain valve 8 and pro desalting water tank 2, also higher than the height of ultrafiltration water tank 3, ensures that the hydrophobic acquisition sufficiently high pressure of steam after raw water heater 1 heat exchange can enter ultrafiltration water tank 3.
During actual use, at the system cloud gray model initial stage, drain valve 8 is opened, and the steam drainage (or steam water interface) after raw water heater 1 enters steam drainage outlet pipe 5, and enters in the high-order steam drainage outlet pipe 5 arranged through drain valve 8.Because system just puts into operation, hydrophobic middle meeting contains a large amount of suspensions, now opens manual diaphragm valve 11, closes pneumatic diaphragm valve A9 and pneumatic diaphragm valve B10, hydrophobicly drains into hyperfiltration reverse-rinsing through hydrophobic dirt-removing pipe 6 and reclaims in pond 4.After system cloud gray model a period of time (time is by determining after the sampling of water quality analysis in hydrophobic dirt-removing pipe 6), closing manual diaphragm valve 11, controlling the break-make of pneumatic diaphragm valve A9 and pneumatic diaphragm valve B10 according to the monitor signal of electric conductive meter 15.When electrical conductivity higher than reverse osmosis water outlet of the monitor signal of electric conductive meter 15, open pneumatic diaphragm valve B10, close pneumatic diaphragm valve A9, now hydrophobicly enter ultrafiltration water tank 3 through bypass duct 7, and enter counter-infiltration system reuse.When electrical conductivity lower than reverse osmosis water outlet of the monitor signal of electric conductive meter 15, open pneumatic diaphragm valve A9, close pneumatic diaphragm valve B10, hydrophobicly enter pro desalting water tank 2, finally enter desalting system.After system is completely normally run, pneumatic diaphragm valve B10 and manual diaphragm valve 11 are all in closed condition, and pneumatic diaphragm valve A9 opens, and hydrophobicly enter pro desalting water tank 2 through pneumatic diaphragm valve A9 and check-valves A12, realize the recovery to raw water heater steam drainage.
More than show and describe general principle of the present utility model, 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; the just principle of the present utility model described in above-described embodiment and description; under the prerequisite not departing from the utility model spirit and scope, the utility model also has various changes and modifications, and these changes and improvements all fall in claimed scope of the present utility model.The protection domain that the utility model requires is defined by appending claims and equivalent thereof.
Claims (3)
1. for the raw water heater steam drainage recovery device of boiler feed water system, comprise main building jet chimney (16), main building jet chimney (16) access raw water heater (1), raw water heater (1) picks out steam drainage outlet pipe (5), steam drainage outlet pipe (5) is connected to hydrophobic dirt-removing pipe (6), hydrophobic dirt-removing pipe (6) is provided with manual diaphragm valve (11), hydrophobic dirt-removing pipe (6) access hyperfiltration reverse-rinsing reclaims pond (4), it is characterized in that:
Described steam drainage outlet pipe (5) is provided with drain valve (8) and electric conductive meter (15), steam drainage outlet pipe (5) access pro desalting water tank (2), steam drainage outlet pipe (5) is connected to bypass duct (7) and bypass duct (7) is positioned between pro desalting water tank (2) and hydrophobic dirt-removing pipe (6), bypass duct (7) access ultrafiltration water tank (3), pro desalting water tank (2) is connected to chemical deionization system pipeline (17), ultrafiltration water tank (3) is connected to counter-infiltration system pipeline (18), steam drainage outlet pipe (5) is positioned at pro desalting water tank (2) import department and pneumatic diaphragm valve A(9 is installed) and check-valves A(12), bypass duct (7) is positioned at ultrafiltration water tank (3) import department and pneumatic diaphragm valve B(10 is installed) and check-valves B(13).
2. the raw water heater steam drainage recovery device for boiler feed water system according to claim 1, it is characterized in that: described steam drainage outlet pipe (5) is provided with heat indicator (14) and heat indicator (14) is positioned between drain valve (8) and electric conductive meter (15), the data output end of heat indicator (14) is connected with the data input pin of electric conductive meter (15).
3. the raw water heater steam drainage recovery device for boiler feed water system according to claim 1, is characterized in that: described steam drainage outlet pipe (5) is positioned at the height of the pipeline absolute altitude between drain valve (8) and pro desalting water tank (2) higher than pro desalting water tank (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520174791.XU CN204534540U (en) | 2015-03-26 | 2015-03-26 | For the raw water heater steam drainage recovery device of boiler feed water system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520174791.XU CN204534540U (en) | 2015-03-26 | 2015-03-26 | For the raw water heater steam drainage recovery device of boiler feed water system |
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| Publication Number | Publication Date |
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| CN204534540U true CN204534540U (en) | 2015-08-05 |
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| CN201520174791.XU Active CN204534540U (en) | 2015-03-26 | 2015-03-26 | For the raw water heater steam drainage recovery device of boiler feed water system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106524124A (en) * | 2015-09-14 | 2017-03-22 | 新特能源股份有限公司 | Eastern Junggar coal concurrent boiler drainage system |
-
2015
- 2015-03-26 CN CN201520174791.XU patent/CN204534540U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106524124A (en) * | 2015-09-14 | 2017-03-22 | 新特能源股份有限公司 | Eastern Junggar coal concurrent boiler drainage system |
| CN106524124B (en) * | 2015-09-14 | 2018-12-25 | 新特能源股份有限公司 | A kind of quasi- eastern coal direct current cooker drainage system |
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