CN2846406Y - Integrated wet oxided waste water processor - Google Patents
Integrated wet oxided waste water processor Download PDFInfo
- Publication number
- CN2846406Y CN2846406Y CN 200520125976 CN200520125976U CN2846406Y CN 2846406 Y CN2846406 Y CN 2846406Y CN 200520125976 CN200520125976 CN 200520125976 CN 200520125976 U CN200520125976 U CN 200520125976U CN 2846406 Y CN2846406 Y CN 2846406Y
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- heat
- water
- temperature
- waste water
- preheater
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- Expired - Fee Related
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses an integrated wet oxidized waste water processor which belongs to the equipment for industrial waste water treatment, particularly the equipment used for processing the industrial waste water under the condition of high temperature and high pressure. The structure of the device is that the integrated wet oxidized waste water processor is composed of a preheating device, a heater and a fixed bed reactor which are orderly connected from up to down in the same heat-insulating container, wherein the bottom of the preheating device is provided with a waste water inlet, and one-way valves for temperature and pressure control are arranged at the connecting positions between the preheating device and the heater and between the heater and the reactor. A high-temperature water outlet for processed water arranged at the top of the reactor is connected with a water inlet of a heat-exchanging pipe using the reaction heat, the heat-exchanging pipe is arranged in the preheating device, and a water outlet of the heat-exchanging pipe is an air outlet for the processed water. The processor integrates the three sets of devices which are arranged in dispersion in the same heat-insulating container, the reuse of various heat energy is realized and the valve for the temperature and pressure control between the device can be adjusted at any time according to the operational conditions of the devices. The continuous production is ensured, and the processing capacity and the utilization rate of the device are improved.
Description
Affiliated technical field
The utility model belongs to Industrial Wastewater Treatment equipment, particularly handles the equipment of trade effluent under high-temperature and high-pressure conditions.
Background technology
The technology that adopts wet oxidation process to handle trade effluent is in recent years adopted by more and more enterprises, this method for COD concentration at the high density of 25000-200000mg/L, poisonous, deleterious organic industrial sewage, the waste water that can't adopt traditional water technology (biological example chemical technology) to handle has good suitability, but, there are shortcomings such as pipe network complexity, energy consumption height and interruption production for the steam water interface that obtains High Temperature High Pressure usually needs many complete equipments.
Summary of the invention
The purpose of this utility model provide a kind of can be to heat pressurization and carry out the technical scheme of the integration apparatus of oxidation of steam water interface.
The technical solution of the utility model is, integral type wet oxidation wastewater treatment equipment, its structure is: be made up of the preheater, well heater, the fixed-bed reactor that connect successively from bottom to top that are installed in the same insulating container, the waste water import is equipped with in the preheater bottom, temperature, pressure control check valve is equipped with in preheater and well heater, well heater and reactor junction, is positioned at that the high-temperature water outlet connects the water-in of handling the back water pipe and leading to the utilization of Heat of Reaction heat transfer tube of preheater behind the treating water of reactor head, the water outlet of this interchanger is moisture outlet after handling.
Described well heater is equipped with the high-temperature steam heat transfer tube, and the afterheat steam of this heat transfer tube exports the afterheat steam import of leading to the waste heat heat transfer tube that is installed in the preheater through the afterheat steam pipe.
Three complete equipments that the utility model will disperse to install are contained in the same insulating container, in preheater, be provided with utilization of Heat of Reaction heat transfer tube and afterheat heat exchanger, can make full use of the reaction heat and the waste heat of high temperature and high pressure steam after the well heater heat exchange that produce in the oxidizing reaction, realize the utilization again of various heat energy preferably, because organic oxidation is thermopositive reaction, organic concentration in waste water is high to a certain degree (it is generally acknowledged that COD is greater than 70000mg/L), the heat that reaction takes place can be kept the needs of operation, the unloading phase of except that system, do not need to provide in addition energy.Temperature, pressure control valve between the equipment can be regulated at any time according to equipment running condition, guarantees continuous production, improves the processing power and the utilization ratio of equipment.
Description of drawings
Accompanying drawing is a structural representation of the present utility model.
Among the figure, 1. handle back high-temperature water outlet, 2. fixed-bed reactor, 3. catalyzer erecting frame, 4. reactor feed valve, 5. well heater, 6. high-temperature heat exchange tube, 7. high temperature and high pressure steam import, 8. afterheat steam outlet, 9. well heater feed valve, 10 afterheat steam pipes, 11. preheaters, 12. the afterheat steam import, 13. waste heat heat transfer tubes, the outlet of 14. condensing aires, 15. the waste water import, 16. handle back water pipe, 17. thermal insulation layers, 18 utilization of Heat of Reaction heat transfer tubes, 19. water waste heat imports, 20. handle the back moisture outlet.
Embodiment
Embodiment of the present utility model is, as shown in the figure:
Embodiment 1, integral type wet oxidation wastewater treatment equipment, its structure is: by the preheater 11 that connects successively from bottom to top that is installed in the same insulating container 17, well heater 5, fixed-bed reactor 2 are formed, catalyzer erecting frame 3 is housed in the fixed-bed reactor, waste water import 15 is equipped with in the preheater bottom, temperature, pressure control check valve---well heater feed valve 9 is equipped with in preheater and well heater junction, temperature, pressure control check valve---reactor feed valve 4 is equipped with in well heater and reactor junction, is positioned at behind the treating water of reactor head high-temperature water outlet 1 and connects and handle the water-in 19 that back water pipe 16 leads to the utilization of Heat of Reaction heat transfer tube 18 of preheater, the water outlet of this interchanger is for handling back moisture outlet 20.
Claims (2)
1. integral type wet oxidation wastewater treatment equipment, it is characterized in that: form by the preheater, well heater, the fixed-bed reactor that connect successively from bottom to top that are installed in the same insulating container, the waste water import is equipped with in the preheater bottom, temperature, pressure control check valve is equipped with in preheater and well heater, well heater and reactor junction, is positioned at that the high-temperature water outlet connects the water-in of handling the back water pipe and leading to the utilization of Heat of Reaction heat transfer tube of preheater behind the treating water of reactor head, the water outlet of this interchanger is moisture outlet after handling.
2. integral type wet oxidation wastewater treatment equipment according to claim 1, it is characterized in that: described well heater is equipped with the high-temperature steam heat transfer tube, and the afterheat steam of this heat transfer tube exports the water-in that leads to the waste heat heat transfer tube that is installed in the preheater through the afterheat steam pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200520125976 CN2846406Y (en) | 2005-12-19 | 2005-12-19 | Integrated wet oxided waste water processor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200520125976 CN2846406Y (en) | 2005-12-19 | 2005-12-19 | Integrated wet oxided waste water processor |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2846406Y true CN2846406Y (en) | 2006-12-13 |
Family
ID=37511825
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200520125976 Expired - Fee Related CN2846406Y (en) | 2005-12-19 | 2005-12-19 | Integrated wet oxided waste water processor |
Country Status (1)
Country | Link |
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CN (1) | CN2846406Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101624566B (en) * | 2009-08-11 | 2012-07-25 | 广州聚能生物科技有限公司 | Integral feeding device and cell crushing machine using same |
CN102774912A (en) * | 2012-07-20 | 2012-11-14 | 陈银轩 | Water preheating device for water ejection separator |
-
2005
- 2005-12-19 CN CN 200520125976 patent/CN2846406Y/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101624566B (en) * | 2009-08-11 | 2012-07-25 | 广州聚能生物科技有限公司 | Integral feeding device and cell crushing machine using same |
CN102774912A (en) * | 2012-07-20 | 2012-11-14 | 陈银轩 | Water preheating device for water ejection separator |
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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: 20061213 Termination date: 20141219 |
|
EXPY | Termination of patent right or utility model |