CN211141812U - Processing system of hot spring waste water - Google Patents
Processing system of hot spring waste water Download PDFInfo
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- CN211141812U CN211141812U CN201921734650.3U CN201921734650U CN211141812U CN 211141812 U CN211141812 U CN 211141812U CN 201921734650 U CN201921734650 U CN 201921734650U CN 211141812 U CN211141812 U CN 211141812U
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Abstract
The utility model provides a processing system of hot spring waste water, include: the system comprises a wastewater adjusting tank, a biochemical system, a reaction system, a clarifying and filtering tank, a membrane separation system, a concentration and decrement system, a desalination system, an evaporative crystallization system and a chlorine dioxide generator; the wastewater adjusting tank, the biochemical system, the reaction system, the clarifying and filtering tank, the membrane separation system, the concentration and decrement system, the desalination system and the evaporative crystallization system are sequentially connected, and the chlorine dioxide generator is connected with the desalination system. The utility model provides a processing system of hot spring waste water can realize the resourceful treatment of hot spring waste water, realizes changing waste into valuables's purpose to in this process, can not produce any solid useless and liquid useless, in addition, can also prepare through chlorine dioxide generator and obtain chlorine dioxide disinfectant, and utilize chlorine dioxide disinfectant to disinfect the hot spring water.
Description
Technical Field
The utility model belongs to the waste water treatment field especially relates to a processing system of hot spring waste water.
Background
The hot spring water is naturally gushed out from the underground or obtained by artificial drilling, and the total amount of hot spring water resources in China is rich. China's hot spring resource has become one of the industries developed by the current government. The hot spring water contains a large amount of heat and mineral substances, and COD and salt content of the hot spring water are increased after bathing. After recycling, salt and COD can be slowly accumulated. At present, the traditional hot spring water is mainly used for bathing, and then the bathing wastewater is directly discharged into the environment, which causes a certain degree of damage to the surrounding environment.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a hot spring waste water's processing system to the problem mentioned in the background art.
For this reason, the above-mentioned purpose of the present invention is achieved by the following technical solutions:
a hot spring waste water's processing system which characterized in that: the system for treating the hot spring wastewater comprises: the system comprises a wastewater adjusting tank, a biochemical system, a reaction system, a clarifying and filtering tank, a membrane separation system, a concentration and decrement system, a desalination system, an evaporative crystallization system and a chlorine dioxide generator; the wastewater adjusting tank, the biochemical system, the reaction system, the clarifying and filtering tank, the membrane separation system, the concentration and decrement system, the desalination system and the evaporative crystallization system are sequentially connected, and the chlorine dioxide generator is connected with the desalination system.
When adopting above-mentioned technical scheme, the utility model discloses can also adopt or make up and adopt following technical scheme:
as the utility model discloses a preferred technical scheme: the biochemical system comprises: the system comprises a hydrolysis acidification tank, an anaerobic tank, an aerobic tank and an MBR reaction tank, wherein the biochemical system is used for performing biochemical treatment on the wastewater from the wastewater adjusting tank.
As the utility model discloses a preferred technical scheme: the reaction system comprises a sodium hydroxide adding tank and a sodium carbonate adding tank, wherein the inlet of the sodium hydroxide adding tank is connected with the outlet of the biochemical system, and the outlet of the sodium hydroxide adding tank is connected with the inlet of the sodium carbonate adding tank; the sodium hydroxide adding tank is used for removing magnesium ions in the wastewater, and the sodium carbonate adding tank is used for removing calcium ions in the wastewater.
As the utility model discloses a preferred technical scheme: the membrane separation system comprises a ceramic membrane device for removing suspended matters and colloids from wastewater from the clarification filtration tank.
As the utility model discloses a preferred technical scheme: the concentration and decrement system comprises a reverse osmosis device which is used for carrying out concentration and decrement treatment on the wastewater from the membrane separation system.
As the utility model discloses a preferred technical scheme: the desalination system comprises an electrodialysis device, and the electrodialysis device is used for carrying out desalination treatment on the concentrated solution discharged by the concentration and decrement system.
As the utility model discloses a preferred technical scheme: the evaporative crystallization system includes one of a multi-effect evaporator and a mechanical vapor recompression evaporator.
As the utility model discloses a preferred technical scheme: and a fresh water outlet of the desalination system is communicated with an inlet of the concentration and decrement system.
The utility model provides a processing system of hot spring waste water, through the waste water equalizing basin, biochemical system, reaction system, clarification filtering ponds, membrane separation system, concentration decrement system, desalination system, the effective arrangement of evaporation crystal system and chlorine dioxide generator, can realize the resourceful treatment of hot spring waste water, realize changing waste into valuables's purpose, and at this in-process, can not produce any solid useless and liquid useless, in addition, can also prepare through the chlorine dioxide generator and obtain chlorine dioxide disinfectant, and utilize chlorine dioxide disinfectant to carry out disinfection and sterilization to hot spring water.
Drawings
FIG. 1 is a schematic representation of a hot spring wastewater treatment system provided by the present invention;
in the figure: 110-a wastewater conditioning tank; 120-biochemical system; 131-sodium hydroxide adding tank; 132-sodium carbonate adding tank; 140-a clarification filtration tank; 150-ceramic membrane device; 160-a reverse osmosis unit; 170-an electrodialysis unit; 180-evaporative crystallization system; 190-chlorine dioxide generator.
Detailed Description
The invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
A system for treating spa waste water comprising: a wastewater adjusting tank 110, a biochemical system 120, a reaction system, a clarifying and filtering tank 140, a membrane separation system, a concentration and decrement system, a desalination system, an evaporative crystallization system 180 and a chlorine dioxide generator 190; the wastewater adjusting tank 110, the biochemical system 120, the reaction system, the clarifying and filtering tank 140, the membrane separation system, the concentration and decrement system, the desalination system and the evaporative crystallization system 180 are sequentially connected, and the chlorine dioxide generator 190 is connected with the desalination system.
The biochemical system 120 includes: a hydrolysis acidification tank, an anaerobic tank, an aerobic tank, an MBR reaction tank, and a biochemical system 120 for performing biochemical treatment on the wastewater from the wastewater conditioning tank 110.
The reaction system comprises a sodium hydroxide adding tank 131 and a sodium carbonate adding tank 132, wherein the inlet of the sodium hydroxide adding tank 131 is connected with the outlet of the biochemical system 120, and the outlet of the sodium hydroxide adding tank 131 is connected with the inlet of the sodium carbonate adding tank 132; sodium hydroxide solid or solution is added into the sodium hydroxide adding tank 131 to remove magnesium ions in the wastewater, and sodium carbonate solid or solution is added into the sodium carbonate adding tank 132 to remove calcium ions in the wastewater.
The clarification filtration tank 140 is an organic combination of a clarifier and a filtration tank. Namely, a filtering layer (thin filtering layer) is arranged in the clear water area of the clarification tank, and the processes of sedimentation, filtration and the like are integrated in a structure.
The membrane separation system includes a ceramic membrane device 150, and the ceramic membrane device 150 is used to remove suspended matter and colloids from the wastewater from the clarification filtration tank 140.
The concentration and decrement system comprises a reverse osmosis device 160, and the reverse osmosis device 160 is used for performing concentration and decrement treatment on the wastewater from the membrane separation system.
The desalination system comprises an electrodialysis device 170, and the electrodialysis device 170 is used for carrying out desalination treatment on the concentrated solution discharged by the concentration and decrement system.
The evaporative crystallization system 180 includes one of a multiple effect evaporator and a mechanical vapor recompression evaporator.
The fresh water outlet of the electrodialysis device 170 is in communication with the inlet of the reverse osmosis device 160.
The utility model provides a processing system of hot spring waste water, through the waste water equalizing basin, biochemical system, reaction system, clarification filtering ponds, membrane separation system, concentration decrement system, desalination system, the effective arrangement of evaporation crystal system and chlorine dioxide generator, can realize the resourceful treatment of hot spring waste water, realize changing waste into valuables's purpose, and at this in-process, can not produce any solid useless and liquid useless, in addition, can also prepare through the chlorine dioxide generator and obtain chlorine dioxide disinfectant, and utilize chlorine dioxide disinfectant to carry out disinfection and sterilization to hot spring water.
The above detailed description is provided for explaining the present invention, and is only a preferred embodiment of the present invention, but not for limiting the present invention, and any modifications, equivalent replacements, improvements, etc. made by the present invention are within the scope of the present invention.
Claims (8)
1. A hot spring waste water's processing system which characterized in that: the hot spring waste water treatment system comprises: the system comprises a wastewater adjusting tank, a biochemical system, a reaction system, a clarifying and filtering tank, a membrane separation system, a concentration and decrement system, a desalination system, an evaporative crystallization system and a chlorine dioxide generator; the wastewater adjusting tank, the biochemical system, the reaction system, the clarifying and filtering tank, the membrane separation system, the concentration and decrement system, the desalination system and the evaporative crystallization system are sequentially connected, and the chlorine dioxide generator is connected with the desalination system.
2. The system for treating spa waste water according to claim 1 wherein: the biochemical system comprises: the system comprises a hydrolysis acidification tank, an anaerobic tank, an aerobic tank and an MBR reaction tank, wherein the biochemical system is used for performing biochemical treatment on the wastewater from the wastewater adjusting tank.
3. The system for treating spa waste water according to claim 1 wherein: the reaction system comprises a sodium hydroxide adding tank and a sodium carbonate adding tank, wherein the inlet of the sodium hydroxide adding tank is connected with the outlet of the biochemical system, and the outlet of the sodium hydroxide adding tank is connected with the inlet of the sodium carbonate adding tank; the sodium hydroxide adding tank is used for removing magnesium ions in the wastewater, and the sodium carbonate adding tank is used for removing calcium ions in the wastewater.
4. The system for treating spa waste water according to claim 1 wherein: the membrane separation system comprises a ceramic membrane device for removing suspended matters and colloids from wastewater from the clarification filtration tank.
5. The system for treating spa waste water according to claim 1 wherein: the concentration and decrement system comprises a reverse osmosis device which is used for carrying out concentration and decrement treatment on the wastewater from the membrane separation system.
6. The system for treating spa waste water according to claim 1 wherein: the desalination system comprises an electrodialysis device, and the electrodialysis device is used for carrying out desalination treatment on the concentrated solution discharged by the concentration and decrement system.
7. The system for treating spa waste water according to claim 1 wherein: the evaporative crystallization system includes one of a multi-effect evaporator and a mechanical vapor recompression evaporator.
8. The system for treating spa waste water according to claim 1 wherein: and a fresh water outlet of the desalination system is communicated with an inlet of the concentration and decrement system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921734650.3U CN211141812U (en) | 2019-10-16 | 2019-10-16 | Processing system of hot spring waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921734650.3U CN211141812U (en) | 2019-10-16 | 2019-10-16 | Processing system of hot spring waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211141812U true CN211141812U (en) | 2020-07-31 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201921734650.3U Active CN211141812U (en) | 2019-10-16 | 2019-10-16 | Processing system of hot spring waste water |
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| CN (1) | CN211141812U (en) |
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2019
- 2019-10-16 CN CN201921734650.3U patent/CN211141812U/en active Active
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A treatment system for hot spring wastewater Effective date of registration: 20211203 Granted publication date: 20200731 Pledgee: Hangzhou High-tech Financing Guarantee Co.,Ltd. Pledgor: SUNUP ENVIRONMENTAL TECHNOLOGY CO.,LTD. Registration number: Y2021980014035 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20220322 Granted publication date: 20200731 Pledgee: Hangzhou High-tech Financing Guarantee Co.,Ltd. Pledgor: SUNUP ENVIRONMENTAL TECHNOLOGY CO.,LTD. Registration number: Y2021980014035 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A treatment system for hot spring wastewater Effective date of registration: 20220322 Granted publication date: 20200731 Pledgee: Shanghai Guotai Junan Securities Asset Management Co.,Ltd. Pledgor: SUNUP ENVIRONMENTAL TECHNOLOGY CO.,LTD. Registration number: Y2022990000163 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20230131 Granted publication date: 20200731 Pledgee: Shanghai Guotai Junan Securities Asset Management Co.,Ltd. Pledgor: SUNUP ENVIRONMENTAL TECHNOLOGY CO.,LTD. Registration number: Y2022990000163 |