CN108557957A - A kind of processing of stone integrated sewage treating apparatus and its processing method - Google Patents
A kind of processing of stone integrated sewage treating apparatus and its processing method Download PDFInfo
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- CN108557957A CN108557957A CN201810693545.3A CN201810693545A CN108557957A CN 108557957 A CN108557957 A CN 108557957A CN 201810693545 A CN201810693545 A CN 201810693545A CN 108557957 A CN108557957 A CN 108557957A
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- 239000010865 sewage Substances 0.000 title claims abstract description 53
- 239000004575 stone Substances 0.000 title claims abstract description 34
- 238000003672 processing method Methods 0.000 title claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 132
- 238000010926 purge Methods 0.000 claims abstract description 53
- 238000005406 washing Methods 0.000 claims abstract description 53
- 238000000034 method Methods 0.000 claims abstract description 21
- 230000000694 effects Effects 0.000 claims description 5
- 239000012528 membrane Substances 0.000 claims description 2
- 238000007781 pre-processing Methods 0.000 claims 1
- 239000003814 drug Substances 0.000 description 9
- 238000004062 sedimentation Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- 235000013339 cereals Nutrition 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000003311 flocculating effect Effects 0.000 description 2
- 238000002203 pretreatment Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- BVPWJMCABCPUQY-UHFFFAOYSA-N 4-amino-5-chloro-2-methoxy-N-[1-(phenylmethyl)-4-piperidinyl]benzamide Chemical compound COC1=CC(N)=C(Cl)C=C1C(=O)NC1CCN(CC=2C=CC=CC=2)CC1 BVPWJMCABCPUQY-UHFFFAOYSA-N 0.000 description 1
- RZVHIXYEVGDQDX-UHFFFAOYSA-N 9,10-anthraquinone Chemical compound C1=CC=C2C(=O)C3=CC=CC=C3C(=O)C2=C1 RZVHIXYEVGDQDX-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000003082 abrasive agent Substances 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 230000000739 chaotic effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052809 inorganic oxide Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/04—Backflushing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/18—Use of gases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/03—Pressure
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/10—Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/046—Recirculation with an external loop
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses a kind of processing of stone integrated sewage treating apparatus, including：Water tank inlet, inlet valve, inlet gage, macropore film device, flowing water Valve, concentrated water valve, air purge component, washing component, water outlet and backwash water tank, inlet pipeline, outlet pipeline, concentrated water pipeline, washing pipeline, air purge pipeline, wherein water tank inlet is connect by inlet pipeline with macropore film device, and inlet valve and inlet gage are provided on inlet pipeline；Water tank inlet is connect by concentrated water pipeline with macropore film device, and concentrated water valve is provided on concentrated water pipeline；Outlet pipeline is connect with macropore film device and water outlet and backwash water tank respectively, and flowing water Valve is provided on outlet pipeline；Washing component is connect by washing pipeline with macropore film device and water outlet and backwash water tank；Air purge component is connect by air purge pipeline with macropore film device；The invention also discloses a kind of processing of stone integral sewage disposal process, the sewage receipts water rate handled through the invention is higher.
Description
Technical field
The present invention relates to environmental technology field, particularly relate to a kind of processing of stone integrated sewage treating apparatus and its
Processing method.
Background technology
In recent years, increasing year by year with processing of stone enterprise, discharge water increasingly increase, most processing of stone enterprises
Industry is all made of large-scale cutting machining stone slab, in order to improve the service life of cutter and grinding tool, utilizes in process clear
Water cooling cutter and grinding tool, the method to exclude clast and residue, thus generate large amount of sewage.Containing a large amount of in such sewage
Mountain flour, main component include silica (SiO2), calcium carbonate (CaCO3) and other inorganic oxides, a small amount of diamond grit,
Abrasive material particulate, while further including the fragment etc. of silt particle and product packaging material that mill floor rinses.In general, sewage
In suspension content in 2000mg/L~4000mg/L, reach as high as 7000mg/L, although sewage disposal enterprise carry out it is multiple
The project of upgrading and rebuilding, but the exceeded situations of SS are still remained in drainage index, seriously affect downstream beach breeding enterprise and surrounding
Ecological environment.Especially the environmentally friendly supervision group feedback opinion in center requires to improve processing of stone garden sewage treatment plant processing energy up to standard
Power improves emergency processing safeguards system, prevents garden sewage accidental release, protects immediate offshore area mudflat aquaculture environment.
The basic skills of the sewage disposal of stone slab processing at present, mainly there is physical treatment process, method of chemical treatment and bioid
Facture three classes are learned, by polluter separation removal contained in sewage, recycles, or be translated into innocuous substance, makes
Water is purified.In general, the bigger pollutant of grain size can be flocculated by conventional chemical, the method strengthened be removed, through grinding
Study carefully grain size main exceeded part in the pollutant of 3~5um is draining, the pollutant grain size of the range is smaller, in sewage
Can be formed it is stable be similar to colloidal state, conventional coagulation-settlement process and device can not remove.
Therefore, there is an urgent need for a kind of new technologies of design to improve its problem by the present inventor.
Invention content
In order to solve the above technical problems, the present invention provides a kind of processing of stone integrated sewage treating apparatus and its processing
Method.
The technical scheme is that：
A kind of processing of stone integrated sewage treating apparatus, including：Water tank inlet, inlet valve, inlet gage, macropore
Film device, flowing water Valve, concentrated water valve, air purge component, washing component, water outlet and backwash water tank, inlet pipeline, outlet pipeline,
Concentrated water pipeline, washing pipeline, air purge pipeline, wherein the water tank inlet is connected by the inlet pipeline and the macropore film device
It connects, the inlet valve and the inlet gage is provided on the inlet pipeline；The water tank inlet passes through described dense
Water lines are connect with the macropore film device, and the concentrated water valve is provided on the concentrated water pipeline；The outlet pipeline point
It is not connect with the macropore film device and the water outlet and backwash water tank, the flowing water Valve is provided on the outlet pipeline；
The washing component is connect by washing pipeline with the macropore film device and the water outlet and backwash water tank；The air purge component
It is connect with the macropore film device by the air purge pipeline.
Preferably, the air purge component includes air purge valve, air purge wind turbine and air purge pressure gauge.
Preferably, the washing component includes washing valve, washing pressure gauge and washing pump.
Preferably, further include an intake pump, the intake pump is connected to the inlet pipeline.
Preferably, the aperture of the macropore film device is 3~5um.
A kind of processing method based on processing of stone integrated sewage treating apparatus described above, includes the following steps：
S1：Open inlet valve, flowing water Valve and concentrated water valve；
S2：Sewage is delivered to macropore film device by inlet pipeline；
S3：Macropore film device is filtered effect to sewage；
S4：It handles water up to standard and drains into water outlet and backwash water tank, then drain into downstream receiving water body；Processing water not up to standard
It is back to the water tank inlet by concentrated water pipeline.
Preferably, further include following pre-treatment step：
S01：The numerical value for checking inlet gage enters step S02 when it reaches the first intake pressure threshold value；It is on the contrary
Then enter step S1；
S02：It keeps inlet valve and intake pump to be in open state, closes flowing water Valve, open air purge valve, open gas
Wind turbine is washed, air purge operation is carried out；
S03：After air purge, the numerical value of inlet gage is checked again, when it reaches the second intake pressure threshold value, into
Enter step S04；It is on the contrary then enter step S1；
S04：Intake pump and inlet valve are closed, washing valve is opened and washing pumps, water washing operations are carried out, in water washing operations
The pressure value of control washing pressure gauge is less than the first intake pressure threshold value or the second intake pressure threshold value in the process.
Preferably, the first intake pressure threshold value and/or the second intake pressure threshold value are 0.3Mpa.
Preferably,：The time of the air purge operation is 10~20s, and the time of the water washing operations is 1~2min.
Preferably, the step S2 is specifically included：Intake pump is opened, sewage is pumped to from inlet tank through intake pump described big
At the film device of hole.
Using above-mentioned technical proposal, the present invention includes at least following advantageous effect：
Processing of stone integrated sewage treating apparatus of the present invention and its processing method, need not add any medicine
Agent, the exceeded sewage in processing of stone end can be directly entered equipment, and medicament is avoided repeatedly to add cycle, and water outlet SS is less than 1mg/L,
Reach return water rank, saves operation medicament expense.
Description of the drawings
Fig. 1 is the structural schematic diagram of processing of stone integrated sewage treating apparatus of the present invention；
Fig. 2 is processing of stone integrated sewage treating apparatus of the present invention；
Fig. 3 is processing of stone integrated sewage treating apparatus of the present invention.
Wherein：It is water tank inlet 1, intake pump 2, inlet valve 3, inlet gage 4, macropore film device 5, flowing water Valve 6, dense
Penstock 7, air purge pressure gauge 9, air purge wind turbine 10, washing pressure gauge 11, washing pump 12, washing valve 13, goes out air purge valve 8
Water and backwash water tank 14.
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation describes, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
As shown in Figure 1, to meet a kind of processing of stone integrated sewage treating apparatus of the present invention, including：Water tank inlet
1, inlet valve 3, inlet gage 4, macropore film device 5, flowing water Valve 6, concentrated water valve 7, air purge component, washing component, go out
Water and backwash water tank 14, inlet pipeline, outlet pipeline, concentrated water pipeline, washing pipeline, air purge pipeline, wherein the water tank inlet 1
It is connect with the macropore film device 5 by the inlet pipeline, the inlet valve 3 and institute is provided on the inlet pipeline
State inlet gage 4；The water tank inlet 1 is connect by the concentrated water pipeline with the macropore film device 5, in the concentrated water pipe
Road is provided with the concentrated water valve 7；The outlet pipeline respectively with the macropore film device 5 and it is described water outlet and backwash water tank
14 connect, and the flowing water Valve 6 is provided on the outlet pipeline；The washing component passes through washing pipeline and the macroporous membrane
Equipment 5 and the water outlet and backwash water tank 14 connect；The air purge component passes through the air purge pipeline and the macropore film device 5
Connection.
Preferably, the air purge component includes air purge valve 8, air purge wind turbine 10 and air purge pressure gauge 9.
Preferably, the washing component includes washing valve 13, washing pressure gauge 11 and washing pump 12.
Preferably, further include an intake pump 2, the intake pump 2 is connected to the inlet pipeline.
Preferably, the aperture of the macropore film device 5 is 3~5um.
As shown in Fig. 2, to meet a kind of based on processing of stone integrated sewage treating apparatus described above of the present invention
Processing method, include the following steps：
S1：Open inlet valve 3, flowing water Valve 6 and concentrated water valve 7；
S2：Sewage is delivered to macropore film device 5 by inlet pipeline；
S3：Macropore film device 5 is filtered effect to sewage；
S4：It handles water up to standard and drains into water outlet and backwash water tank 14, then drain into downstream receiving water body；Processing is not up to standard
Water is back to the water tank inlet 1 by concentrated water pipeline.
Preferably, further include following pre-treatment step：
S01：The numerical value for checking inlet gage 4 enters step S02 when it reaches the first intake pressure threshold value；It is on the contrary
Then enter step S1；
S02：It keeps inlet valve 3 and intake pump 2 to be in open state, closes flowing water Valve 6, open air purge valve 8, open
Air purge wind turbine 10 is opened, air purge operation is carried out；
S03：After air purge, the numerical value of inlet gage 4 is checked again, when it reaches the second intake pressure threshold value,
Enter step S04；It is on the contrary then enter step S1；
S04：Intake pump 2 and inlet valve 3 are closed, washing valve 13 and washing pump 12 is opened, water washing operations is carried out, in water
The pressure value for washing control washing pressure gauge 11 in operating process is less than the first intake pressure threshold value or second influent pressure
Force threshold.
Preferably, the first intake pressure threshold value and/or the second intake pressure threshold value are 0.3Mpa.
Preferably,：The time of the air purge operation is 10~20s, and the time of the water washing operations is 1~2min.
Preferably, the step S2 is specifically included：Intake pump 2 is opened, sewage is pumped to from inlet tank through intake pump 2 described
At macropore film device 5.
The processing of stone integrated equipment for sewage treatment receives water rate up to 90%, i.e., with gauge of intaking, 90% ratio into
Water can only will produce 10% concentrated water in the process with qualified discharge or recycling, which may return to original
Water intake pool continues with.
But as film device uses the increase of duration to need to carry out when 4 pressure of inlet gage increases to 0.3Mpa
Gas back-flushing, specific operation process are to keep inlet valve 3 and 2 open state of intake pump, close flowing water Valve 6, open gas
Wash valve 8, be then turned on air purge wind turbine 10, air purge pressure gauge 9 is controlled during air purge and is less than 0.1Mpa, when macroscopically feel into
Stop air purge when water and the similar ss suspended solid of water outlet, it is considered that air purge process continues 10~20s.When discovery air purge
Ineffective, i.e., air purge is completed, and inlet gage 4 is washed at this time still in 0.3Mpa or so when intaking again, is had
Body water-washing process is to close intake pump 2, closes inlet valve 3, opens washing valve 13, is controlled during opening washing pump 12
It washes 11 pressure of pressure gauge and is less than 0.3Mpa, wash 1~2min.
Processing of stone sewage water is big, and major pollutants are solid suspension SS and a small amount of organic matter cooling for cut
Liquid, conventional treatment process mainly select horizontal sedimentation tank, vertical sedimentation tank monomer or technique are used in conjunction, and can add in processing procedure
Enter a large amount of coagulating sedimentation medicaments, since ss suspended solid is very high in sewage, precipitation process will produce a large amount of sludge, and dehydration link needs
Flocculation aid is added again, and squeezing draining needs to return into water to handle again, and different types of precipitation medicament is in sewage disposal system
Internal constantly cycle, causes water outlet ss suspended solid especially grain size to form a kind of state of stabilization in the fine particle of 3~5um,
Not free settling, end adds precipitation medicament almost without flocculating effect again, or even sewage treatment facility can be made to go out water chaotic degree
It increases.Processing of stone sewage integrated treatment device of the present invention is using intake pump 2, macropore film device 5, air purge wind turbine 10, washing
The capital equipments such as pump 12.In conjunction with sewage collecting pool, intake pump room 2, vertical sedimentation tank, horizontal sedimentation tank, sewage regulating reservoir, sheet frame
Sludge conditioning pond, plate and frame filter press, the centrifugally regulated pond of sludge, sludge centrifuge etc., can in conjunction with attached processing step shown in Fig. 3
To avoid the generation of above-mentioned phenomenon.Solid arrow indicates that water route, dotted arrow indicate road, please know in Fig. 3.
Main advantage of the present invention is as follows：
(1) any medicament need not be added, the exceeded sewage in processing of stone end can be directly entered equipment, avoid medicament more
Secondary to add cycle, water outlet SS is less than 1mg/L, reaches recycle-water rank, saved operation medicament expense；
(2) water rate height is received compared to conventional film product, ton water cost of investment is low；
(3) since flocculating effect is good, so filter effect is substantially better than traditional physical filtering equipment (such as sand filtration apparatus)；
(4) compared to traditional gravity stream filtering or no pressure stream filtration system, this equipment uses pressure filtration, belongs to
Pressure flow, can be taking human as the size of control inflow, emergency flight control when being significantly increased as water fluctuation and rainy season water
System.
The foregoing description of the disclosed embodiments enables those skilled in the art to implement or use the present invention.
Various modifications to these embodiments will be apparent to those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, of the invention
It is not intended to be limited to the embodiments shown herein, and is to fit to and the principles and novel features disclosed herein phase one
The widest range caused.
Claims (10)
1. a kind of processing of stone integrated sewage treating apparatus, which is characterized in that including：Water tank inlet, inlet valve, influent pressure
Power table, macropore film device, flowing water Valve, concentrated water valve, air purge component, washing component, water outlet and backwash water tank, inlet pipeline,
Outlet pipeline, concentrated water pipeline, washing pipeline, air purge pipeline, wherein the water tank inlet by the inlet pipeline with it is described big
Hole film device connection, is provided with the inlet valve and the inlet gage on the inlet pipeline；The water tank inlet
It is connect with the macropore film device by the concentrated water pipeline, the concentrated water valve is provided on the concentrated water pipeline；It is described
Outlet pipeline is connect with the macropore film device and the water outlet and backwash water tank respectively, is provided on the outlet pipeline described
Flowing water Valve；The washing component is connect by washing pipeline with the macropore film device and the water outlet and backwash water tank；Institute
Air purge component is stated to connect with the macropore film device by the air purge pipeline.
2. processing of stone integrated sewage treating apparatus as described in claim 1, it is characterised in that：The air purge component includes
Air purge valve, air purge wind turbine and air purge pressure gauge.
3. processing of stone integrated sewage treating apparatus as claimed in claim 1 or 2, it is characterised in that：The washing component
Including washing valve, washing pressure gauge and washing pump.
4. processing of stone integrated sewage treating apparatus as described in any one of claims 1-3, it is characterised in that：Further include one into
Water pump, the intake pump are connected to the inlet pipeline.
5. the processing of stone integrated sewage treating apparatus as described in claim 1-4 is any, it is characterised in that：The macroporous membrane
The aperture of equipment is 3~5um.
6. a kind of processing method based on any processing of stone integrated sewage treating apparatus of claim 1-5, special
Sign is, includes the following steps：
S1：Open inlet valve, flowing water Valve and concentrated water valve；
S2：Sewage is delivered to macropore film device by inlet pipeline；
S3：Macropore film device is filtered effect to sewage；
S4：It handles water up to standard and drains into water outlet and backwash water tank, then drain into downstream receiving water body；Processing water not up to standard passes through
Concentrated water pipeline is back to the water tank inlet.
7. processing of stone integral sewage disposal process as claimed in claim 6, which is characterized in that further include pre-processing as follows
Step：
S01：The numerical value for checking inlet gage enters step S02 when it reaches the first intake pressure threshold value；It is on the contrary then into
Enter step S1；
S02：It keeps inlet valve and intake pump to be in open state, closes flowing water Valve, open air purge valve, open air purge wind
Machine carries out air purge operation；
S03：After air purge, the numerical value of inlet gage is checked again, when it reaches the second intake pressure threshold value, into step
Rapid S04；It is on the contrary then enter step S1；
S04：Intake pump and inlet valve are closed, washing valve is opened and washing pumps, water washing operations are carried out, in water washing operations process
The pressure value of middle control washing pressure gauge is less than the first intake pressure threshold value or the second intake pressure threshold value.
8. processing of stone integral sewage disposal process as claimed in claim 7, it is characterised in that：First intake pressure
Threshold value and/or the second intake pressure threshold value are 0.3Mpa.
9. processing of stone integral sewage disposal process as claimed in claim 7 or 8, it is characterised in that：The air purge operation
Time be 10~20s, time of the water washing operations is 1~2min.
10. the processing of stone integral sewage disposal process as described in claim 6-9 is any, it is characterised in that：The step
S2 is specifically included：Intake pump is opened, sewage is pumped to from the macropore film device from inlet tank through intake pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810693545.3A CN108557957B (en) | 2018-06-29 | 2018-06-29 | Stone processing integrated sewage treatment device and treatment method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810693545.3A CN108557957B (en) | 2018-06-29 | 2018-06-29 | Stone processing integrated sewage treatment device and treatment method thereof |
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| Publication Number | Publication Date |
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| CN108557957A true CN108557957A (en) | 2018-09-21 |
| CN108557957B CN108557957B (en) | 2023-10-24 |
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| CN201810693545.3A Active CN108557957B (en) | 2018-06-29 | 2018-06-29 | Stone processing integrated sewage treatment device and treatment method thereof |
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