CN201507917U - Exhaust recovery device of deaerator - Google Patents
Exhaust recovery device of deaerator Download PDFInfo
- Publication number
- CN201507917U CN201507917U CN2009202283885U CN200920228388U CN201507917U CN 201507917 U CN201507917 U CN 201507917U CN 2009202283885 U CN2009202283885 U CN 2009202283885U CN 200920228388 U CN200920228388 U CN 200920228388U CN 201507917 U CN201507917 U CN 201507917U
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- packed tower
- communicated
- deaerator
- hot water
- water
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Abstract
An exhaust recovery device of a deaerator comprises a packed tower casing, wherein padding in the packed tower casing is divided into an upper padding layer and a lower padding layer, the top portion of the packed tower casing is provided with an exhaust vent, a cold water inlet is arranged on the upper portion of the packed tower casing, a steam inlet and a hot water outlet are arranged on the lower portion of the packed tower casing in turn, a circulating hot water inlet is arranged on the packed tower casing between the upper padding layer and the lower padding layer, one end of a water outlet pipeline is communicated with the hot water outlet, and the other end thereof is respectively communicated with inlets of two water pumps, the outlets of the two water pumps are communicated with the circulating hot water inlet, a pipeline between two water pumps is communicated with a water inlet pipe of a deaerator, the upper and the lower padding layers are regular, and the water pump is centrifugal. The exhaust recovery device of the deaerator provided by the utility model can recycle heat energy in steam exhausted by the deaerator, reduces the atmospheric emission, saves energy sources, protects environment, and has simple structure and convenient use.
Description
Technical field
The utility model relates to a kind of boiler heat-energy recovering apparatus, particularly a kind of exhaust recovery device of deaerator.
Background technology
In the production process of industrial enterprise that boiler is arranged and electric power enterprise, the deoxygenation mode of boiler feedwater adopts the thermal de-aeration mode usually, to guarantee the quality of feedwater.This deoxygenation mode has simply, the reliable and good advantage of deaerating effect, but the steam that oxygen-eliminating device produces generally directly is discharged in the atmosphere, has not only increased the airborne release amount, and environment is caused thermal pollution, and contained heat is not utilized in the steam, has wasted the energy.According to measuring and calculating, 100 tons the air suspended type oxygen-eliminating device of exerting oneself, under normal operation, water temperature reaches 104 ℃ and oxygen-eliminating device internal pressure and reaches 0.02MPa when above in the oxygen-eliminating device, the quantity of steam that per hour is discharged into atmosphere reaches the 0.5-0.7 ton, under the situation that intensification and recycling economy transform,, will produce huge economic benefit at present world energy supplies growing tension and China as and if being used with this part Steam Recovery.
Summary of the invention
Technical problem to be solved in the utility model provides a kind of exhaust recovery device of deaerator, and the heat in the steam that it can be discharged the recycling oxygen-eliminating device has reduced the airborne release amount, has saved the energy, has protected environment, and is simple in structure, easy to use.
In order to solve the problems of the technologies described above, the technical solution of the utility model is: a kind of exhaust recovery device of deaerator, comprise the packed tower housing, filler in the packed tower housing is divided into packing layer and following packing layer, the packed tower case top is provided with exhaust outlet, packed tower housing top is provided with cooling water inlet, the packed tower lower housing portion is provided with steam inlet and hot water outlet successively, the circulating hot water import is located on the packed tower housing between packing layer and the following packing layer, outlet conduit one end is communicated with hot water outlet, the outlet conduit other end is communicated with the import of two water pumps respectively, the outlet of two water pumps is communicated with the circulating hot water import, and the pipeline between two water pumps is communicated with the oxygen-eliminating device water inlet pipe.
Last packing layer and following packing layer are structured filling material layer.
Water pump is a centrifugal pump.
A kind of exhaust recovery device of deaerator that the utility model provides, with the place of packed tower as recovery oxygen-eliminating device discharged steam heat, after in packed tower, injecting the heat of cold desalted water recovery oxygen-eliminating device discharged steam, sending packed tower back to after water pump will pressurize from the hot desalted water that packed tower comes out recycles, sending oxygen-eliminating device back to after other has the hot desalted water that reaches temperature standard of small part to be pressurizeed by water pump uses, the oxygen-eliminating device steam consumption is significantly descended, and energy-saving effect is obvious; Also can eliminate the air pollution that produces to atmospheric exhaust because of directly, protect environment; Simple in structure, easy to operate, safe and reliable to operation.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples.
Fig. 1 is a structural representation of the present utility model.
The specific embodiment
As shown in Figure 1, the utility model comprises packed tower housing 2, filler in the packed tower housing 2 is divided into packing layer 9 and following packing layer 10, packed tower housing 2 tops are provided with exhaust outlet 1, packed tower housing 2 tops are provided with cooling water inlet 3, packed tower housing 2 bottoms are provided with steam inlet 5 and hot water outlet 6 successively, circulating hot water import 4 is located on the packed tower housing 2 between packing layer 9 and the following packing layer 10, outlet conduit 11 1 ends are communicated with hot water outlet 6, and outlet conduit 11 other ends are communicated with the import of two water pumps 7,7 ' respectively, two water pumps 7,7 ' outlet is communicated with circulating hot water import 4, two water pumps 7, and the pipeline between 7 ' is communicated with oxygen-eliminating device water inlet pipe 8.
The course of work of the present utility model is as follows:
In the cooling water inlet 3 on packed tower housing 2 tops, inject cold desalted water, the steam that oxygen-eliminating device is discharged is from bottom that steam inlet 5 is introduced packed tower housings 2, cold desalted water enters in the packed tower from the cooling water inlet 3 on packed tower housing 2 tops, the Steam Heating that is entered in the dropping process of cold desalted water packing layer 9 and following packing layer 10 on process is at last by hot water outlet 6 outflows; Fixed gas enters atmosphere from the exhaust outlet 1 at packed tower housing 2 tops, the hot desalted water that flows out from hot water outlet 6 is through water pump 7,7 ' pressurization is after circulating hot water import 4 is sent back to the heat that continues to absorb steam in the packed tower housing 2, and the portion of hot desalted water is sent back to oxygen-eliminating device through oxygen-eliminating device water inlet pipe 8 and used.
Claims (3)
1. exhaust recovery device of deaerator, comprise packed tower housing (2), filler in the packed tower housing (2) is divided into packing layer (9) and following packing layer (10), packed tower housing (2) top is provided with exhaust outlet (1), packed tower housing (2) top is provided with cooling water inlet (3), packed tower housing (2) bottom is provided with steam inlet (5) and hot water outlet (6) successively, it is characterized in that: circulating hot water import (4) is located on the packed tower housing (2) between packing layer (9) and the following packing layer (10), outlet conduit (11) one ends are communicated with hot water outlet (6), outlet conduit (11) other end respectively with two water pumps (7,7 ') import is communicated with, two water pumps (7,7 ') outlet is communicated with circulating hot water import (4), and the pipeline between two water pumps (7,7 ') is communicated with oxygen-eliminating device water inlet pipe (8).
2. a kind of exhaust recovery device of deaerator according to claim 1 is characterized in that: going up packing layer (9) and following packing layer (10) is structured filling material layer.
3. a kind of exhaust recovery device of deaerator according to claim 1 is characterized in that: water pump (7,7 ') is a centrifugal pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009202283885U CN201507917U (en) | 2009-09-25 | 2009-09-25 | Exhaust recovery device of deaerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009202283885U CN201507917U (en) | 2009-09-25 | 2009-09-25 | Exhaust recovery device of deaerator |
Publications (1)
Publication Number | Publication Date |
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CN201507917U true CN201507917U (en) | 2010-06-16 |
Family
ID=42469044
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2009202283885U Expired - Lifetime CN201507917U (en) | 2009-09-25 | 2009-09-25 | Exhaust recovery device of deaerator |
Country Status (1)
Country | Link |
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CN (1) | CN201507917U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101666487B (en) * | 2009-09-25 | 2012-05-30 | 湖北华强化工集团有限公司 | Exhaust recovery device of deaerator |
CN106606916A (en) * | 2015-10-26 | 2017-05-03 | 安徽华尔泰化工股份有限公司 | Sulfur melting steam recovery and utilization apparatus |
-
2009
- 2009-09-25 CN CN2009202283885U patent/CN201507917U/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101666487B (en) * | 2009-09-25 | 2012-05-30 | 湖北华强化工集团有限公司 | Exhaust recovery device of deaerator |
CN106606916A (en) * | 2015-10-26 | 2017-05-03 | 安徽华尔泰化工股份有限公司 | Sulfur melting steam recovery and utilization apparatus |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20100616 Effective date of abandoning: 20090925 |