CN206255949U - A kind of power-plant waste processing equipment - Google Patents
A kind of power-plant waste processing equipment Download PDFInfo
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- CN206255949U CN206255949U CN201621326769.3U CN201621326769U CN206255949U CN 206255949 U CN206255949 U CN 206255949U CN 201621326769 U CN201621326769 U CN 201621326769U CN 206255949 U CN206255949 U CN 206255949U
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- exchange bed
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- fan
- firing equipment
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Abstract
This application discloses a kind of power-plant waste processing equipment, it is made up of flowmeter, filter, firing equipment, cation exchange bed, carbon dioxide cleaner, water tank, water pump, anion exchange bed, output equipment and valve, flowmeter is connected with filter, the filter is connected with firing equipment, cation exchange bed is connected with firing equipment, and carbon dioxide cleaner difference cation exchange bed is connected with water tank；Sodium ion removal effect is good, sodium ions content 15 × 10‑8mg/L；It is abundant to calcium ion removal, calcium ion content 15 × 10‑7mg/L；Carbon dioxide content is low, and dioxide-containing silica is 37 × 10‑8mg/L；It is excellent to chlorion removal effect, chloride ion content 48 × 10‑8mg/L；It is abundant to magnesium ion removal, magnesium ion content 0.5 4.5 × 10‑7mg/L；Sulfate ion content is processed low, sulfate ion content 26 × 10‑8mg/L。
Description
Technical field
The application is related to sewage treatment equipment field, more particularly to a kind of power-plant waste processing equipment.
Background technology
Wastewater treatment（wastewater treatment methods）It is exactly the method pair using physics, chemistry and biology
Waste water is processed, and makes purification of waste water, reduces pollution, so that reaching Sewage treatment, multiplexing, makes full use of water resource.
Separated by physical action, reclaim the undissolved pollutant in suspended state in waste water（Including oil film and oil droplet）
Waste water treatment process, gravitational separation process, centrifugal separation and sieving retention method etc. can be divided into.Place based on heat exchange principle
Logos falls within physical treatment process.
Separate, remove by chemical reaction and effect of mass transmitting in waste water in dissolving, the pollutant of colloidal state or by its
It is converted into the waste water treatment process of innocuous substance.In method of chemical treatment, to add the treatment based on medicament produces chemical reaction
Unit is：Coagulation, neutralization, redox etc.；And the processing unit based on effect of mass transmitting then has：Extraction, stripping, stripping,
Absorption, ion exchange and electrodialysis and counter-infiltration etc..Latter two processing unit is collectively referred to as membrane separation technique again.Wherein with biography
The processing unit of matter effect both has chemical action, there is associated physical action again, so also can chemically in facture
Branch away, as another kind of processing method, referred to as physical-chemical process.
By the metabolism of microorganism, make the organic pollution in solution, colloid and fine suspended state in waste water,
It is converted into stabilization, the waste water treatment process of harmless material.According to the difference of effect microorganism, biological treatment can be divided into aerobic again
Biological treatment and anaerobic bio-treated two types.Biological wastewater treatment is widely used that aerobe facture, traditionally,
Aerobe facture is divided into activated sludge process and the class of biomembrance process two again.Inherently a kind of processing unit of activated sludge process,
It has various methods of operation.Belong to the processing equipment of biomembrance process have biofilter, biological rotating disk, biological contact oxidation pond and
Biological fluidized bed etc..Bio-oxidation pond method is also known as natural ecological resource method.Anaerobic biotreatment method, also known as biological reducing treatment
Method, mainly for the treatment of high concentrated organic wastewater and sludge.The processing equipment for using predominantly digester.
Waste water is processed with biological contact oxidation process, i.e., filler is filled in biological reaction pool with Biological Contact Oxidation Process,
The whole fillers of sewage submergence of oxygenation, and filler is flowed through with certain flow velocity.It is covered with biomembrane, sewage and life on filler
Thing film is contacted extensively, and on the biomembrane in the presence of the metabolism of microorganism, dirty organic pollutants are removed, sewage
It is purified.Finally, treated waste water is entered after biological contact oxidization treatment system mixes with sanitary sewage and processed, chlorine
Qualified discharge after sterilization.Biological contact oxidation process is a kind of biomembrance process work between activated sludge process and biofilter
Skill, is characterized in setting filler in pond, and bottom of pond aeration carries out oxygenation to sewage, and sewage in pond body is in flow regime,
To ensure that sewage is fully contacted with the filler being immersed in sewage, it is to avoid there is sewage in biological contact oxidation pond and contacted with filler
Uneven defect, this aerator appellation blast aeration.
Microbiological fuel cell processing method, malicious class thing is carried out using the microorganism of the degraded waste being inoculated with fuel cell
Matter, organic matter, the degraded of impurity.Common microbiological fuel cell can be divided into：Single-chamber microbial fuel cell, double-chamber microbiological
Fuel cell.
Utility model content
The technical problem of solution：
The application technical issues that need to address are that removal sodium ion, calcium ion and magnesium ion are insufficient in the prior art,
Dioxide-containing silica is high, the excessively high technical problem of chlorion, carbon dioxide, sulfate ion equal size, proposes a kind of power plant's heat
Electric system spends the sewage treatment equipment except good purification.
Technical scheme：
A kind of power-plant waste processing equipment, by flowmeter, filter, firing equipment, cation exchange bed, carbon dioxide cleaner,
Water tank, water pump, anion exchange bed, output equipment and valve composition, the flowmeter are provided with waste water input port, flowmeter with
Filter is connected, and activated carbon filter layer is provided with filter, and the filter is connected with firing equipment, and firing equipment bottom is provided with
Resistive heater, cation exchange bed is connected with firing equipment, and carbon dioxide cleaner difference cation exchange bed is connected with water tank, on water tank
Water pump is provided with, the water in water tank is transferred in anion exchange bed by water pump, anion exchange bed is connected with output equipment,
The output equipment is provided with valve.
As a kind of optimal technical scheme of the application：The firing equipment one side top is provided with fan, just to fan
One side be provided with passage and be connected with cation exchange bed.
As a kind of optimal technical scheme of the application：The downward-sloping 20-40 ° of angle of firing equipment top surface and cation
Exchange the connection of bed side.
As a kind of optimal technical scheme of the application：It is described just to the top blow-by of the one side of fan, with cation
The passage for exchanging bed connection is located at the top of just to the one side of fan.
As a kind of optimal technical scheme of the application：It is described just to the passage on the one side of fan and firing equipment top
Face is parallel.
Beneficial effect：
A kind of herein described power-plant waste processing equipment using above technical scheme compared with prior art, with
Lower technique effect：1st, sodium ion removal effect is good, sodium ions content 1-5 × 10-8mg/L；2nd, it is abundant to calcium ion removal, calcium from
Sub- content 1-5 × 10-7mg/L；3rd, carbon dioxide content is low, and dioxide-containing silica is 3-7 × 10-8mg/L；4th, chlorion is gone
Except excellent effect, chloride ion content 4-8 × 10-8mg/L；5th, it is abundant to magnesium ion removal, magnesium ion content 0.5-4.5 × 10- 7mg/L；6th, sulfate ion content has been processed low, sulfate ion content 2-6 × 10-8Mg/L, can be used widely, not
It is disconnected to substitute current material.
Brief description of the drawings：
Fig. 1 is the structural representation of the application power-plant waste processing equipment.
Description of reference numerals：1st, flowmeter, 2, filter, 3, firing equipment, 4, cation exchange bed, 5, carbon dioxide cleaner, 6,
Water tank, 7, water pump, 8, anion exchange bed, 9, output equipment, 10, valve, 11, waste water delivery outlet, 12, activated carbon filter layer,
13rd, resistive heater, 14, fan.
Specific embodiment
Following examples further illustrate present context, but should not be construed as the limitation to the application.Without departing substantially from
In the case of the application spirit and essence, the modification and replacement made to the application method, step or condition belong to the application
Scope.
If not specializing, the conventional meanses that technological means used is well known to those skilled in the art in embodiment.
Embodiment 1:
As shown in figure 1, a kind of power-plant waste processing equipment, is handed over by flowmeter 1, filter 2, firing equipment 3, cation
Change bed 4, carbon dioxide cleaner 5, water tank 6, water pump 7, anion exchange bed 8, output equipment 9 and valve 10 to constitute, set on the flowmeter
Have waste water input port 11, flowmeter is connected with filter 2, be provided with activated carbon filter layer 12 in filter 2, the filter 2 with
Firing equipment 3 is connected, and the one side of firing equipment 3 top is provided with fan 14, and the just one side to fan 14 is provided with passage with sun
Ion exchange bed 4 is connected, and just to the one side top blow-by of fan 14, the passage being connected with cation exchange bed 4 is located at just
To the one side top of fan 14, the bottom of firing equipment 3 is provided with resistive heater 13, the downward-sloping 20 ° of angles of the top surface of firing equipment 3
It is connected with the side of cation exchange bed 4, just parallel with the top surface of firing equipment 3 to the passage on the one side of fan 14, carbon dioxide cleaner 5
Cation exchange bed 4 is connected with water tank 6 respectively, and water tank 6 is provided with water pump 7, and the water in water tank 6 is transferred into the moon by water pump 7
In ion exchange bed 8, anion exchange bed 8 is connected with output equipment 9, and the output equipment 9 is provided with valve 10.
Sodium ion removal effect is good, sodium ions content 5 × 10-8mg/L；It is abundant to calcium ion removal, calcium ion content 5 ×
10-7mg/L；Carbon dioxide content is low, and dioxide-containing silica is 7 × 10-8mg/L；It is excellent to chlorion removal effect, chlorion
Content 8 × 10-8mg/L；It is abundant to magnesium ion removal, magnesium ion content 4.5 × 10-7mg/L；Sulfate ion content is processed
It is low, sulfate ion content 6 × 10-8Mg/L, can be used widely, and constantly substitute current material.
Embodiment 2：
As shown in figure 1, a kind of power-plant waste processing equipment, is handed over by flowmeter 1, filter 2, firing equipment 3, cation
Change bed 4, carbon dioxide cleaner 5, water tank 6, water pump 7, anion exchange bed 8, output equipment 9 and valve 10 to constitute, set on the flowmeter
Have waste water input port 11, flowmeter is connected with filter 2, be provided with activated carbon filter layer 12 in filter 2, the filter 2 with
Firing equipment 3 is connected, and the one side of firing equipment 3 top is provided with fan 14, and the just one side to fan 14 is provided with passage with sun
Ion exchange bed 4 is connected, and just to the one side top blow-by of fan 14, the passage being connected with cation exchange bed 4 is located at just
To the one side top of fan 14, the bottom of firing equipment 3 is provided with resistive heater 13, the downward-sloping 25 ° of angles of the top surface of firing equipment 3
It is connected with the side of cation exchange bed 4, just parallel with the top surface of firing equipment 3 to the passage on the one side of fan 14, carbon dioxide cleaner 5
Cation exchange bed 4 is connected with water tank 6 respectively, and water tank 6 is provided with water pump 7, and the water in water tank 6 is transferred into the moon by water pump 7
In ion exchange bed 8, anion exchange bed 8 is connected with output equipment 9, and the output equipment 9 is provided with valve 10.
Sodium ion removal effect is good, sodium ions content 4 × 10-8mg/L；It is abundant to calcium ion removal, calcium ion content 4 ×
10-7mg/L；Carbon dioxide content is low, and dioxide-containing silica is 6 × 10-8mg/L；It is excellent to chlorion removal effect, chlorion
Content 7 × 10-8mg/L；It is abundant to magnesium ion removal, magnesium ion content 3.5 × 10-7mg/L；Sulfate ion content is processed
It is low, sulfate ion content 5 × 10-8Mg/L, can be used widely, and constantly substitute current material.
Embodiment 3:
As shown in figure 1, a kind of power-plant waste processing equipment, is handed over by flowmeter 1, filter 2, firing equipment 3, cation
Change bed 4, carbon dioxide cleaner 5, water tank 6, water pump 7, anion exchange bed 8, output equipment 9 and valve 10 to constitute, set on the flowmeter
Have waste water input port 11, flowmeter is connected with filter 2, be provided with activated carbon filter layer 12 in filter 2, the filter 2 with
Firing equipment 3 is connected, and the one side of firing equipment 3 top is provided with fan 14, and the just one side to fan 14 is provided with passage with sun
Ion exchange bed 4 is connected, and just to the one side top blow-by of fan 14, the passage being connected with cation exchange bed 4 is located at just
To the one side top of fan 14, the bottom of firing equipment 3 is provided with resistive heater 13, the downward-sloping 35 ° of angles of the top surface of firing equipment 3
It is connected with the side of cation exchange bed 4, just parallel with the top surface of firing equipment 3 to the passage on the one side of fan 14, carbon dioxide cleaner 5
Cation exchange bed 4 is connected with water tank 6 respectively, and water tank 6 is provided with water pump 7, and the water in water tank 6 is transferred into the moon by water pump 7
In ion exchange bed 8, anion exchange bed 8 is connected with output equipment 9, and the output equipment 9 is provided with valve 10.
Sodium ion removal effect is good, sodium ions content 3 × 10-8mg/L；It is abundant to calcium ion removal, calcium ion content 3 ×
10-7mg/L；Carbon dioxide content is low, and dioxide-containing silica is 5 × 10-8mg/L；It is excellent to chlorion removal effect, chlorion
Content 6 × 10-8mg/L；It is abundant to magnesium ion removal, magnesium ion content 2.5 × 10-7mg/L；Sulfate ion content is processed
It is low, sulfate ion content 4 × 10-8Mg/L, can be used widely, and constantly substitute current material.
Embodiment 4:
As shown in figure 1, a kind of power-plant waste processing equipment, is handed over by flowmeter 1, filter 2, firing equipment 3, cation
Change bed 4, carbon dioxide cleaner 5, water tank 6, water pump 7, anion exchange bed 8, output equipment 9 and valve 10 to constitute, set on the flowmeter
Have waste water input port 11, flowmeter is connected with filter 2, be provided with activated carbon filter layer 12 in filter 2, the filter 2 with
Firing equipment 3 is connected, and the one side of firing equipment 3 top is provided with fan 14, and the just one side to fan 14 is provided with passage with sun
Ion exchange bed 4 is connected, and just to the one side top blow-by of fan 14, the passage being connected with cation exchange bed 4 is located at just
To the one side top of fan 14, the bottom of firing equipment 3 is provided with resistive heater 13, the downward-sloping 40 ° of angles of the top surface of firing equipment 3
It is connected with the side of cation exchange bed 4, just parallel with the top surface of firing equipment 3 to the passage on the one side of fan 14, carbon dioxide cleaner 5
Cation exchange bed 4 is connected with water tank 6 respectively, and water tank 6 is provided with water pump 7, and the water in water tank 6 is transferred into the moon by water pump 7
In ion exchange bed 8, anion exchange bed 8 is connected with output equipment 9, and the output equipment 9 is provided with valve 10.
Sodium ion removal effect is good, sodium ions content 2 × 10-8mg/L；It is abundant to calcium ion removal, calcium ion content 2 ×
10-7mg/L；Carbon dioxide content is low, and dioxide-containing silica is 4 × 10-8mg/L；It is excellent to chlorion removal effect, chlorion
Content 5 × 10-8mg/L；It is abundant to magnesium ion removal, magnesium ion content 1.5 × 10-7mg/L；Sulfate ion content is processed
It is low, sulfate ion content 3 × 10-8Mg/L, can be used widely, and constantly substitute current material.
Embodiment 5：
As shown in figure 1, a kind of power-plant waste processing equipment, is handed over by flowmeter 1, filter 2, firing equipment 3, cation
Change bed 4, carbon dioxide cleaner 5, water tank 6, water pump 7, anion exchange bed 8, output equipment 9 and valve 10 to constitute, set on the flowmeter
Have waste water input port 11, flowmeter is connected with filter 2, be provided with activated carbon filter layer 12 in filter 2, the filter 2 with
Firing equipment 3 is connected, and the one side of firing equipment 3 top is provided with fan 14, and the just one side to fan 14 is provided with passage with sun
Ion exchange bed 4 is connected, and just to the one side top blow-by of fan 14, the passage being connected with cation exchange bed 4 is located at just
To the one side top of fan 14, the bottom of firing equipment 3 is provided with resistive heater 13, the downward-sloping 30 ° of angles of the top surface of firing equipment 3
It is connected with the side of cation exchange bed 4, just parallel with the top surface of firing equipment 3 to the passage on the one side of fan 14, carbon dioxide cleaner 5
Cation exchange bed 4 is connected with water tank 6 respectively, and water tank 6 is provided with water pump 7, and the water in water tank 6 is transferred into the moon by water pump 7
In ion exchange bed 8, anion exchange bed 8 is connected with output equipment 9, and the output equipment 9 is provided with valve 10.
Sodium ion removal effect is good, sodium ions content 1 × 10-8mg/L；It is abundant to calcium ion removal, calcium ion content 1 ×
10-7mg/L；Carbon dioxide content is low, and dioxide-containing silica is 3 × 10-8mg/L；It is excellent to chlorion removal effect, chlorion
Content 4 × 10-8mg/L；It is abundant to magnesium ion removal, magnesium ion content 0.5 × 10-7mg/L；Sulfate ion content is processed
It is low, sulfate ion content 2 × 10-8Mg/L, can be used widely, and constantly substitute current material.
Presently filed embodiment is explained in detail above in conjunction with accompanying drawing, but the application is not limited to above-mentioned implementation
Mode, in the ken that those of ordinary skill in the art possess, can also be on the premise of the application objective not be departed from
Make a variety of changes.
Claims (5)
1. a kind of power-plant waste processing equipment, it is characterised in that：The power-plant waste processing equipment is by flowmeter（1）, mistake
Filter（2）, firing equipment（3）, cation exchange bed（4）, carbon dioxide cleaner（5）, water tank（6）, water pump（7）, anion exchange bed
（8）, output equipment（9）And valve（10）Composition, the flowmeter is provided with waste water input port（11）, flowmeter and filter
（2）It is connected, filter（2）Inside it is provided with activated carbon filter layer（12）, the filter（2）With firing equipment（3）It is connected, heating sets
It is standby（3）Bottom is provided with resistive heater（13）, cation exchange bed（4）With firing equipment（3）It is connected, carbon dioxide cleaner（5）It is positive respectively
Ion exchange bed（4）And water tank（6）It is connected, water tank（6）It is provided with water pump（7）, by water pump（7）By water tank（6）In water turn
Move on to anion exchange bed（8）It is interior, anion exchange bed（8）With output equipment（9）It is connected, the output equipment（9）It is provided with
Valve（10）.
2. a kind of power-plant waste processing equipment according to claim 1, it is characterised in that：The firing equipment（3）One
Side top is provided with fan（14）, just to fan（14）One side be provided with passage and cation exchange bed（4）Connection.
3. a kind of power-plant waste processing equipment according to claim 2, it is characterised in that：The firing equipment（3）Top
20-40 ° of angle and cation exchange bed are inclined downwards（4）Side connects.
4. a kind of power-plant waste processing equipment according to claim 2, it is characterised in that：It is described just to fan（14）'s
One side top blow-by, with cation exchange bed（4）The passage of connection is located at just to fan（14）One side top.
5. a kind of power-plant waste processing equipment according to claim 2, it is characterised in that：It is described just to fan（14）'s
Passage and firing equipment on one side（3）Top surface is parallel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621326769.3U CN206255949U (en) | 2016-12-06 | 2016-12-06 | A kind of power-plant waste processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621326769.3U CN206255949U (en) | 2016-12-06 | 2016-12-06 | A kind of power-plant waste processing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206255949U true CN206255949U (en) | 2017-06-16 |
Family
ID=59029699
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621326769.3U Expired - Fee Related CN206255949U (en) | 2016-12-06 | 2016-12-06 | A kind of power-plant waste processing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206255949U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110486968A (en) * | 2019-08-28 | 2019-11-22 | 中南大学 | One kind being based on CO2The combined cooling and power system of working medium |
| CN110590035A (en) * | 2019-08-28 | 2019-12-20 | 伊犁川宁生物技术有限公司 | MVR falling film evaporation water production treatment system and process thereof |
-
2016
- 2016-12-06 CN CN201621326769.3U patent/CN206255949U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110486968A (en) * | 2019-08-28 | 2019-11-22 | 中南大学 | One kind being based on CO2The combined cooling and power system of working medium |
| CN110590035A (en) * | 2019-08-28 | 2019-12-20 | 伊犁川宁生物技术有限公司 | MVR falling film evaporation water production treatment system and process thereof |
| CN110486968B (en) * | 2019-08-28 | 2021-01-26 | 中南大学 | Based on CO2Combined cooling and power system for working medium |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Zhong Jianwei Inventor after: Wu Zuofu Inventor before: You Wei Inventor before: Yang Yanzong |
|
| CB03 | Change of inventor or designer information | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20171114 Address after: 538000 Guangxi port city of Fangchenggang Dongxing District Road No. 663 Tian Industrial Zone Fangchenggang yameiju stone building materials market investment Limited by Share Ltd office building 2 room 206 Patentee after: Fangchenggang Huixin agricultural science and Technology Co., Ltd. Address before: 214000 Jiangsu, Xishan District, northeast of the town of agricultural dam Industrial Park Patentee before: Wuxi Longying Environmental Protection Technology Co., Ltd. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170616 Termination date: 20171206 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |