CN206191624U - High -load organic matter sewage burns heat cascade utilization's processing apparatus - Google Patents
High -load organic matter sewage burns heat cascade utilization's processing apparatus Download PDFInfo
- Publication number
- CN206191624U CN206191624U CN201621111445.8U CN201621111445U CN206191624U CN 206191624 U CN206191624 U CN 206191624U CN 201621111445 U CN201621111445 U CN 201621111445U CN 206191624 U CN206191624 U CN 206191624U
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- Prior art keywords
- boiler
- temperature heat
- heat pipe
- pipe
- pipeline
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The utility model discloses a high -load organic matter sewage burns heat cascade utilization's processing apparatus, it includes high -temperature heat pipe, medium temperature heat pipe, tubular heat exchanger, boiler and steam pocket, high -temperature heat pipe be two sets of to arrange the setting from top to bottom, wherein, the output that is located the high -temperature heat pipe of below links to each other with medium temperature heat pipe, medium temperature heat pipe output and tubular heat exchanger's input link to each other, the boiler sets up in medium temperature heat pipe top, and is equipped with the fin on the outer wall of medium temperature heat pipe and boiler, the steam pocket be located the top of boiler the steam pocket on be equipped with first pipeline, second pipeline and third pipeline. The utility model discloses overall structure is compact, enables the temperature and forms the organic matter of step type in to sewage and handle, and the heat that forms in every link simultaneously can both effectively be utilized.
Description
Technical field
The utility model is related to sewage-treatment plant, more particularly to a kind of high content organic matter sewage to burn heat step profit
Processing unit.
Background technology
With continuing to develop for industry, industrial wastewater (sewage) is also need to be effectively addressed one of important.Due to
Contain substantial amounts of organic matter (generally including phenols, aldehydes, carbohydrate, polysaccharide, protein and oils etc.) in waste water；Also one gives up
Can also be containing poisonous pollutant (such as in water：Organic agricultural chemicals, Polychlorinated biphenyls, carcinogen, petroleum hydrocarbons).If directly
Into after air, soil, water system, serious harm will be produced to animals and plants and human body.Although at present to the processing method of waste water, state
It is inside and outside all to have made substantial amounts of research, but traditional physics, physical chemistry, chemistry, electrochemical method can not be all reached to waste water
In organic matter carry out complete, efficient treatment.
Utility model content
The utility model is to avoid the weak point existing for above-mentioned prior art, there is provided a kind of high content organic matter is dirty
Water burns the processing unit of heat cascade utilization.
The utility model solves the technical scheme that is used of technical problem：
A kind of high content organic matter sewage burns the processing unit of heat cascade utilization, and it includes high-temperature heat pipe, middle warm
Pipe, tubular heat exchanger, boiler and drum, described high-temperature heat pipe are two groups, and the setting that is arranged above and below, wherein, it is underlying
The output end of high-temperature heat pipe is connected with moderate temperature heat pipe, and described moderate temperature heat pipe output end is connected with the input of tubular heat exchanger,
The boiler is arranged on moderate temperature heat pipe top, and moderate temperature heat pipe is provided with fin with the outer wall of boiler, and described drum is located at pot
The top of stove, is provided with the first pipeline, second pipe and the 3rd pipeline on described drum；
First pipeline and second pipe connect with boiler respectively, in described the 3rd pipeline and high temperature above
Heat pipe connects；
The heat absorption evaporation ends of underlying high-temperature heat pipe are provided with combustion chamber, the output end of high-temperature heat pipe above
It is connected with the combustion chamber on underlying high-temperature heat pipe by hot back tube；
Oil gas vent is additionally provided with described boiler side top；
Boiler tube is provided with described tubular heat exchanger, described boiler tube is helically set in tubular heat exchanger, and the stove
The input of pipe is stretched out outside tubular heat exchanger, and its output end is also stretched out outside tubular heat exchanger and is connected with boiler.
Further, natural gas entrance and oil gas entrance are additionally provided with the input of described combustion chamber.
Further, the surface of two groups of high-temperature heat pipes is provided with fin.
Further, first pipeline is connected with boiler top, and the second pipe inserts boiler internal, and second pipe
Lower end is near boiler inner bottom part.
Further, the tubular heat exchanger is also associated with blowdown stack.
Utility model works step is as follows：
Step 1, natural gas is sprayed into the combustion chamber of high-temperature heat pipe front end, make natural gas in burning Indoor Combustion and produce
High temperature, its high temperature passes sequentially through high-temperature heat pipe, moderate temperature heat pipe and tubular heat exchanger and is emitted by blowdown stack；
Step 2, by sewage by boiler tube and by tubular heat exchanger enter boiler in and heat；
Step 3, when the sewage in boiler reaches boiling, many micro-bubbles can be formed, under bubble constitute water,
Gas, oil droplet three-phase heterodisperse system, gas-oil droplet knot is formed in the presence of interfacial tension, bubble floating power and hydrostatic pressure difference
Zoarium floats, and is discharged by oil gas vent standby；
Step 4 and water, gas in step 3 are then entered in drum by the first pipeline, now in the effect of high temperature in drum
Lower generation pressure simultaneously forms the high temperature globule and high-temperature gas；
Step 5, the high temperature globule are flowed into boiler by second pipe, and high-temperature gas is then passed into by the 3rd pipeline
Reused in high-temperature heat pipe above, and in returning to combustion chamber by hot back tube together with the high temperature in high-temperature heat pipe.
Further, the temperature in described combustion chamber is 700-900 DEG C.
Further, the temperature in described high-temperature heat pipe is 800-850 DEG C.
Further, the temperature in the moderate temperature heat pipe is 250-350 DEG C.
Further, the temperature in the tubular heat exchanger (3) is 200 DEG C.
Compared with the prior art, the beneficial effects of the utility model are embodied in：
The utility model compact overall structure, can make temperature form ladder-type and the organic matter in sewage is processed, together
When each link in formed heat can be utilized effectively.
Brief description of the drawings
Fig. 1 is the utility model first embodiment structural representation；
Fig. 2 is the utility model second embodiment structural representation.
Specific embodiment
In order that technological means, creation characteristic, reached purpose and effect that the utility model is realized are easy to understand, under
Face combines and is specifically illustrating, and the utility model is expanded on further.
Embodiment one
As described in Figure 1, a kind of high content organic matter sewage burns the processing unit of heat cascade utilization, and it includes high warm
Pipe 1, moderate temperature heat pipe 2, tubular heat exchanger 3, boiler 4 and drum 5, described high-temperature heat pipe 1 are two groups (101,102), and up and down
Spread configuration, wherein, the output end of underlying high-temperature heat pipe 102 is connected with moderate temperature heat pipe 2, and described moderate temperature heat pipe 2 is defeated
Go out end to be connected with the input of tubular heat exchanger 3, the boiler 4 is arranged on the top of moderate temperature heat pipe 2, and moderate temperature heat pipe 2 and boiler 4
Outer wall be provided with fin 24, described drum 5 is located at the top of boiler 4, be provided with described drum 5 first pipeline 51,
The pipeline 53 of second pipe 52 and the 3rd；First pipeline 51 and second pipe 52 connect with boiler 4 respectively, the described the 3rd
Pipeline 53 connects with high-temperature heat pipe 101 above；The heat absorption evaporation ends of underlying high-temperature heat pipe 102 are provided with burning
Room 100, the output end of high-temperature heat pipe 101 above is by the burning on hot back tube 6 and underlying high-temperature heat pipe 102
Room 100 is connected；Oil gas vent 40 is additionally provided with the described side of boiler 4 top；Boiler tube is provided with described tubular heat exchanger 3
30, described boiler tube 30 is helically set in tubular heat exchanger 3, and the input of the boiler tube 30 is stretched out outside tubular heat exchanger 3,
Its output end is also stretched out outside tubular heat exchanger 3 and is connected with boiler 4.
Natural gas entrance 7 and oil gas entrance 8 are additionally provided with the input of described combustion chamber 100.
The surface of two groups of high-temperature heat pipes (101,102) is provided with fin 25.
First pipeline 51 is connected with the top of boiler 4, inside the insertion boiler 4 of the second pipe 52, and second pipe
52 lower ends are near the inner bottom part of boiler 4.
The tubular heat exchanger 3 is also associated with blowdown stack 9.
Utility model works step is as follows：
Step 1, natural gas is sprayed into the combustion chamber 100 of high-temperature heat pipe 101 front end, make natural gas in combustion chamber 100
High temperature is burnt and produces, its high temperature passes sequentially through high-temperature heat pipe 101, moderate temperature heat pipe 2 and tubular heat exchanger 3 and by blowdown stack 9
Emit；
Step 2, by sewage by boiler tube 30 and by tubular heat exchanger 3 into boiler 4 and heating；
Step 3, when the sewage in boiler 4 reaches boiling, many micro-bubbles can be formed, under bubble constitute
Water, gas, oil droplet three-phase heterodisperse system, gas-oil droplet is formed in the presence of interfacial tension, bubble floating power and hydrostatic pressure difference
Combination floats, and is discharged by oil gas vent 40 standby；
Step 4 and water, gas in step 3 are then entered in drum 5 by the first pipeline 51, now in high temperature in drum 5
Effect is lower to be produced pressure and forms the high temperature globule and high-temperature gas；
Step 5, the high temperature globule are flowed into boiler 4 by second pipe 52, and high-temperature gas then passes through the 3rd pipeline 53
It is passed into high-temperature heat pipe 101 above, and burning is returned to by hot back tube 6 together with the high temperature in high-temperature heat pipe 101
Reused in room 100.
Temperature in described combustion chamber 100 is 700-900 DEG C.Temperature in described high-temperature heat pipe 1 is 800-850
℃.Temperature in the moderate temperature heat pipe 2 is 250-350 DEG C.Temperature in the tubular heat exchanger 3 is 200 DEG C.
Embodiment two
As shown in Fig. 2 the present embodiment two is with the difference of embodiment one, described oil gas vent 40 passes through pipeline 11
It is connected with injector (not shown) with oil gas entrance 8.Combustion medium in the combustion chamber 100 is oil gas.
General principle of the present utility model, principal character and advantage has been shown and described above.The technical staff of the industry
It should be appreciated that the utility model is not restricted to the described embodiments, the simply explanation described in above-described embodiment and specification is originally
The principle of utility model, on the premise of the utility model spirit and scope are not departed from, the utility model also has various change
And improvement, these changes and improvements are both fallen within the range of claimed the utility model.The utility model claims scope
By appending claims and its equivalent thereof.
Claims (5)
1. a kind of high content organic matter sewage burns the processing unit of heat cascade utilization, it is characterised in that：It includes high warm
Pipe (1), moderate temperature heat pipe (2), tubular heat exchanger (3), boiler (4) and drum (5), described high-temperature heat pipe (1) for two groups (101,
102), and the setting that is arranged above and below, wherein, the output end of underlying high-temperature heat pipe (102) is connected with moderate temperature heat pipe (2), institute
Moderate temperature heat pipe (2) output end stated is connected with the input of tubular heat exchanger (3), and the boiler (4) is arranged on moderate temperature heat pipe (2)
Top, and moderate temperature heat pipe (2) is provided with fin (24) with the outer wall of boiler (4), described drum (5) is positioned at the upper of boiler (4)
Side, is provided with the first pipeline (51), second pipe (52) and the 3rd pipeline (53) on described drum (5)；
First pipeline (51) and second pipe (52) connect with boiler (4) respectively, in the 3rd described pipeline (53) and position
High-temperature heat pipe (101) in top connects；
The heat absorption evaporation ends of underlying high-temperature heat pipe (102) are provided with combustion chamber (100), high-temperature heat pipe above
(101) output end is connected by hot back tube (6) with the combustion chamber (100) on underlying high-temperature heat pipe (102)；
Oil gas vent (40) is additionally provided with described boiler (4) side top；
Boiler tube (30) is provided with described tubular heat exchanger (3), described boiler tube (30) helically sets in tubular heat exchanger (3)
Put, and the input of the boiler tube (30) stretches out tubular heat exchanger (3) outward, its output end also stretch out tubular heat exchanger (3) outward and with
Boiler (4) is connected.
2. a kind of high content organic matter sewage according to claim 1 burns the processing unit of heat cascade utilization, and it is special
Levy and be：Natural gas entrance (7) and oil gas entrance (8) are additionally provided with the input of described combustion chamber (100).
3. a kind of high content organic matter sewage according to claim 1 burns the processing unit of heat cascade utilization, and it is special
Levy and be：The surface of two groups of high-temperature heat pipes (101,102) is provided with fin (25).
4. a kind of high content organic matter sewage according to claim 1 burns the processing unit of heat cascade utilization, and it is special
Levy and be：First pipeline (51) is connected with boiler (4) top, and the second pipe (52) insertion boiler (4) is internal, and the
Two pipelines (52) lower end is near boiler (4) inner bottom part.
5. a kind of high content organic matter sewage according to claim 1 burns the processing unit of heat cascade utilization, and it is special
Levy and be：The tubular heat exchanger (3) is also associated with blowdown stack (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621111445.8U CN206191624U (en) | 2016-10-11 | 2016-10-11 | High -load organic matter sewage burns heat cascade utilization's processing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621111445.8U CN206191624U (en) | 2016-10-11 | 2016-10-11 | High -load organic matter sewage burns heat cascade utilization's processing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206191624U true CN206191624U (en) | 2017-05-24 |
Family
ID=58730806
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621111445.8U Withdrawn - After Issue CN206191624U (en) | 2016-10-11 | 2016-10-11 | High -load organic matter sewage burns heat cascade utilization's processing apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206191624U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106439883A (en) * | 2016-10-11 | 2017-02-22 | 安徽国孚润滑油工业有限公司 | Treatment device and method for high-content organic matter sewage incineration heat gradient utilization |
-
2016
- 2016-10-11 CN CN201621111445.8U patent/CN206191624U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106439883A (en) * | 2016-10-11 | 2017-02-22 | 安徽国孚润滑油工业有限公司 | Treatment device and method for high-content organic matter sewage incineration heat gradient utilization |
| CN106439883B (en) * | 2016-10-11 | 2019-01-11 | 安徽国孚润滑油工业有限公司 | A kind of high-content organic matter sewage burns the processing unit and method of heat cascade utilization |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170524 Effective date of abandoning: 20190111 |