CN106336029A - Mobile sewage treatment device and control method - Google Patents
Mobile sewage treatment device and control method Download PDFInfo
- Publication number
- CN106336029A CN106336029A CN201610868660.0A CN201610868660A CN106336029A CN 106336029 A CN106336029 A CN 106336029A CN 201610868660 A CN201610868660 A CN 201610868660A CN 106336029 A CN106336029 A CN 106336029A
- Authority
- CN
- China
- Prior art keywords
- area
- water
- valve
- membrane module
- filtering area
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 15
- 239000010865 sewage Substances 0.000 title claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 63
- 239000012528 membrane Substances 0.000 claims abstract description 42
- 238000001914 filtration Methods 0.000 claims abstract description 36
- 239000002351 wastewater Substances 0.000 claims abstract description 22
- 238000000746 purification Methods 0.000 claims abstract description 9
- 239000000463 material Substances 0.000 claims abstract description 4
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 6
- 229910052571 earthenware Inorganic materials 0.000 claims description 4
- 238000001223 reverse osmosis Methods 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 4
- 239000004411 aluminium Substances 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 230000003139 buffering effect Effects 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 238000007654 immersion Methods 0.000 claims description 3
- 230000008595 infiltration Effects 0.000 claims description 3
- 238000001764 infiltration Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 229910021645 metal ion Inorganic materials 0.000 claims description 3
- 230000003647 oxidation Effects 0.000 claims description 3
- 238000007254 oxidation reaction Methods 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 238000005245 sintering Methods 0.000 claims description 3
- 230000001954 sterilising effect Effects 0.000 claims description 3
- 238000000108 ultra-filtration Methods 0.000 claims description 3
- 208000002447 Macrophagic myofasciitis Diseases 0.000 abstract 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 1
- 239000000919 ceramic Substances 0.000 abstract 1
- 229910010272 inorganic material Inorganic materials 0.000 abstract 1
- 239000011147 inorganic material Substances 0.000 abstract 1
- 238000005192 partition Methods 0.000 abstract 1
- 241000196324 Embryophyta Species 0.000 description 7
- 238000004140 cleaning Methods 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 241000519996 Teucrium chamaedrys Species 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 239000000725 suspension Substances 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
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
-
- 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
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- 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
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- 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
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- 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
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1268—Membrane bioreactor systems
Abstract
The invention discloses a mobile sewage treatment device and a control method. The mobile sewage treatment device comprises a shell, wherein the shell is partitioned into a pretreatment area, a membrane component filtering area and an effluent purification area through partitions; external wastewater is conveyed to the pretreatment area through a conveying pump; the pretreatment area is connected with the membrane component filtering area through a pipeline; the membrane component filtering area is connected with the effluent purification area through another pipeline; a membrane component in the membrane component filtering area is an inorganic material ceramic plate membrane which is made of an alumina material in a sintered manner; the membrane component filtering area is an MMF treatment system, a membrane bioreactor MBR or an MBR treatment system. The mobile sewage treatment device is convenient to wash, small in floor space, convenient to transport, relatively good in treated water quality and good in operation reliability.
Description
Technical field
The present invention relates to a kind of package plant and method.
Background technology
Because Environmental protection in recent years is increasingly paid attention to, the process of sewage has become as the problem of China's concern,
The sewage and waste water amount of some midget plants is less at present, if building a sewage treatment facility, the income of factory may be produced
Raw loss, floor space accordingly increases, and the investment demand for factory increases, and it also requires some technology assistant director is regularly right
Sewage treatment facility is overhauled, and increases difficulty to shop.And some large-scale plant effuent amounts are larger, or occur applying
Work goes wrong, and sewage treatment facility treatment effeciency is slow, then need a kind of sewage treatment facility that should be acute.
Mobile sewage treatment apparatus are removed using current the most efficient materialization, biology and membrane filtration handling process, collection
Ss, heavy metal, cod, bod5、nh3, he is widely used in the fields such as electronic circuit board, plating, medical treatment, cell to-n.
It, by the comprehensive utilization of sewage treatment process, better processing effect, takes up an area less, operation more aspect.Existing portable dirty
It is not good enough often to there is membrane component cleaning performance in water treatment facilities, the features such as cleaning is more difficult, leads to the water treatment efficiency not to be
Highly desirable.
Content of the invention
The technical problem to be solved in the present invention is to provide a kind of operational reliability high, the more preferably portable sewage of water quality treatment
Processing meanss and control method.
In order to solve above-mentioned technical problem, the present invention takes technical scheme below:
A kind of package plant, described device includes housing, is separated into pretreating zone, film by dividing plate in this housing
Component filters area and water outlet purifying area, extraneous waste water is pumped into pretreating zone through conveying, pretreating zone pass through pipeline with
Membrane module filtering area connects, and membrane module filtering area is connected with water outlet purifying area by pipeline.
Membrane module in described membrane module filtering area is using the inorganic earthenware slab film of oxidation aluminium material sintering.
Described membrane module filtering area is mmf processing system, membrane bioreactor mbr or immersion ultra-filtration filters membrane module.
Described membrane module filtering area and water outlet purify interval and are additionally provided with buffering area.
Described water outlet purifying area is provided with switch board and filter, be provided with this filter water intaking valve, anti-valve, counter enter valve,
Positive valve and produce water valve, water intaking valve and anti-valve are connected in series by pipeline, positive valve and produce water valve be connected in parallel rear and counter enter
Valve is connected in series.
Described water outlet purifying area is provided with ro reverse osmosis treatment device.
Described water outlet purifying area is provided with ozone generator and air blast, and this air blast passes through pipeline with membrane module filtering area even
Connect.
A kind of control method of package plant, comprises the following steps:
Waste water is delivered in pretreating zone and is pre-processed, adjust the ph value of waste water, make metal ion in waste water produce reaction shape
Become the particle bigger than ionic condition；
Again waste water is delivered in membrane module filtering area and filter, carry out separation of solid and liquid；
Again water is delivered in water outlet purifying area, carrying out out from water outlet purifying area is detected, satisfactory discharged,
Undesirable, it is re-introduced in pretreating zone.
Specifically include in described water outlet purifying area: using filter, filtration, purification is carried out again to water；Or it is anti-using ro
Infiltration processing meanss carry out filtration, purification again to water；Or using ozone generator, sterilizing is carried out to water.
The present invention adopts inorganic earthenware slab film, and filtering accuracy can reach 0.1 μm, and more traditional membrane component is not only
There is treatment effect good, and easy cleaning, the features such as easy to maintenance.Simplify technical process, floor space is little, and operational reliability carries
Height, water quality treatment are more preferably, easy for installation, are readily transported.
Brief description
Accompanying drawing 1 is the structural representation of the embodiment one of apparatus of the present invention；
Accompanying drawing 2 is the structural representation of the embodiment two of apparatus of the present invention；
Accompanying drawing 3 is the structural representation of the embodiment three of apparatus of the present invention.
Specific embodiment
For the ease of the understanding of those skilled in the art, the invention will be further described below in conjunction with the accompanying drawings.
Embodiment one, as shown in Figure 1, a kind of package plant, described device includes housing, in this housing
Pretreating zone 1, membrane module filtering area 2 and water outlet purifying area 4 are separated into by dividing plate, extraneous waste water is pumped into through conveying
Pretreating zone 1, pretreating zone is connected with membrane module filtering area 2 by 1 pipeline, and it is net with water outlet that membrane module filtering area 2 passes through pipeline
Change area 4 to connect.Membrane module in membrane module filtering area is using the inorganic earthenware slab film of oxidation aluminium material sintering.Film
Component filters area is mmf processing system, and the membrane module that is, staple fibre is made filters.Membrane module filtering area and water outlet purify interval
It is additionally provided with buffering area 3.Water outlet purifying area 4 is provided with switch board 5 and filter 6, be provided with this filter 6 water intaking valve 7, anti-valve 8,
Counter enter valve 9, positive valve 10 and produce water valve 11, water intaking valve and anti-valve are connected in series by pipeline, positive valve and produce water valve parallel connection
After connection with counter enter valve be connected in series.The impurity such as bacterium in eliminating water, microorganism and suspension, the water after purification can effectively be removed
As clear as crystal, turbidity is bordering on zero.By anti-valve, counter enter valve, positive valve and produce the controlling so that qualified water is from producing water of water valve
Valve is discharged, and underproof water is then discharged to pretreating zone again from positive valve and anti-valve.The place of especially suitable heavy metal wastewater thereby
Reason.
Effectively embodiment two, as shown in Figure 2, this embodiment two and the difference of embodiment one are: membrane module filtering area
For immersion ultra-filtration filters membrane module, and it is provided with ro reverse osmosis treatment device 12 in water outlet purifying area 4.Especially suitable heavy metal
The process of waste water.By this ro reverse osmosis treatment device, can effectively go dissolved solids in eliminating water, organic matter, colloid, microorganism
And the impurity such as bacterium.Have the advantages that applied range, high degree of automation, take up an area less, energy consumption is low, effluent quality is preferable.
Embodiment three, as shown in Figure 3, this embodiment three and the difference of embodiment one are: membrane module filtering area is film
Bioreactor mbr, water outlet purifying area is provided with ozone generator 13 and air blast 14, and this air blast passes through pipeline and membrane module mistake
Filter area connects.The process of especially suitable organic wastewater.
Additionally, first collecting in feeder waste water, then convey the effective conveying it is ensured that waste water by delivery pump.
Additionally, present invention further teaches a kind of control method of package plant, comprising the following steps:
S1, waste water is delivered in pretreating zone and is pre-processed, and adjusts the ph value of waste water, makes metal ion in waste water produce reaction
Form the particle bigger than ionic condition；
S2, then waste water is delivered to filtration in membrane module filtering area, carry out separation of solid and liquid；
S3, then water is delivered in water outlet purifying area, carrying out out from water outlet purifying area is detected, satisfactory is arranged
Put, undesirable, it is re-introduced in pretreating zone.
Specifically include in described water outlet purifying area: using filter, filtration, purification is carried out again to water；Or it is anti-using ro
Infiltration processing meanss carry out filtration, purification again to water；Or using ozone generator, sterilizing is carried out to water.
It should be noted that the above is not limited to the present invention, in the creation design without departing from the present invention
Under the premise of, any obvious replacement is all within protection scope of the present invention.
Claims (9)
1. a kind of package plant, it is characterised in that described device includes housing, is separated by dividing plate in this housing
Become pretreating zone, membrane module filtering area and water outlet purifying area, extraneous waste water is pumped into pretreating zone through conveying, pretreatment
Area is connected with membrane module filtering area by pipeline, and membrane module filtering area is connected with water outlet purifying area by pipeline.
2. package plant according to claim 1 is it is characterised in that film in described membrane module filtering area
Assembly is using the inorganic earthenware slab film of oxidation aluminium material sintering.
3. package plant according to claim 2 is it is characterised in that described membrane module filtering area is mmf
Processing system, membrane bioreactor mbr or immersion ultra-filtration filters membrane module.
4. package plant according to claim 3 is it is characterised in that described membrane module filtering area and water outlet
Purify interval and be additionally provided with buffering area.
5. package plant according to claim 4 is it is characterised in that described water outlet purifying area is provided with control
Cabinet and filter, be provided with this filter water intaking valve, anti-valve, counter enter valve, positive valve and produce water valve, water intaking valve and anti-valve lead to
Cross pipeline to be connected in series, positive valve and produce water valve be connected in parallel after and counter enter valve be connected in series.
6. package plant according to claim 4 it is characterised in that described water outlet purifying area to be provided with ro anti-
Infiltration processing meanss.
7. package plant according to claim 4 is it is characterised in that described water outlet purifying area is provided with ozone
Generator and air blast, this air blast is connected with membrane module filtering area by pipeline.
8. a kind of control method of the package plant according to any one of claim 1-7, including following
Step:
Waste water is delivered in pretreating zone and is pre-processed, adjust the ph value of waste water, make metal ion in waste water produce reaction shape
Become the particle bigger than ionic condition；
Again waste water is delivered in membrane module filtering area and filter, carry out separation of solid and liquid；
Again water is delivered in water outlet purifying area, carrying out out from water outlet purifying area is detected, satisfactory discharged,
Undesirable, it is re-introduced in pretreating zone.
9. a kind of control method of mobile work sewage-treatment plant according to claim 8 it is characterised in that described go out
Water warfare specifically includes in area: carries out filtration, purification using filter again to water；Or utilize ro reverse osmosis treatment device pair
Water carries out filtration, purification again；Or using ozone generator, sterilizing is carried out to water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610868660.0A CN106336029A (en) | 2016-09-30 | 2016-09-30 | Mobile sewage treatment device and control method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610868660.0A CN106336029A (en) | 2016-09-30 | 2016-09-30 | Mobile sewage treatment device and control method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106336029A true CN106336029A (en) | 2017-01-18 |
Family
ID=57839635
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610868660.0A Pending CN106336029A (en) | 2016-09-30 | 2016-09-30 | Mobile sewage treatment device and control method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106336029A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02164500A (en) * | 1988-12-19 | 1990-06-25 | Meidensha Corp | Water purifying treatment apparatus |
| CN101734815A (en) * | 2009-12-23 | 2010-06-16 | 苏州市环境工程有限责任公司 | Electronic electroplating wastewater recycling advanced treatment technology |
| CN101880097A (en) * | 2010-01-18 | 2010-11-10 | 王鹤立 | Method and device for moving and quickly treating heavy metal-containing polluted water |
| CN202322530U (en) * | 2011-11-17 | 2012-07-11 | 苏州新区星火环境净化有限公司 | Vehicle-mounted sewage treatment system |
| CN103102025A (en) * | 2013-01-29 | 2013-05-15 | 江西省城乡规划设计研究院 | Method for online recovering heavy metal resource from heavy metal waste water |
| US20140339173A1 (en) * | 2013-05-15 | 2014-11-20 | Fnmc Environmental Inc. | Mining apparatus with water reclamation system |
-
2016
- 2016-09-30 CN CN201610868660.0A patent/CN106336029A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02164500A (en) * | 1988-12-19 | 1990-06-25 | Meidensha Corp | Water purifying treatment apparatus |
| CN101734815A (en) * | 2009-12-23 | 2010-06-16 | 苏州市环境工程有限责任公司 | Electronic electroplating wastewater recycling advanced treatment technology |
| CN101880097A (en) * | 2010-01-18 | 2010-11-10 | 王鹤立 | Method and device for moving and quickly treating heavy metal-containing polluted water |
| CN202322530U (en) * | 2011-11-17 | 2012-07-11 | 苏州新区星火环境净化有限公司 | Vehicle-mounted sewage treatment system |
| CN103102025A (en) * | 2013-01-29 | 2013-05-15 | 江西省城乡规划设计研究院 | Method for online recovering heavy metal resource from heavy metal waste water |
| US20140339173A1 (en) * | 2013-05-15 | 2014-11-20 | Fnmc Environmental Inc. | Mining apparatus with water reclamation system |
Non-Patent Citations (1)
| Title |
|---|
| 李同川: "《化工原理实践指导》", 31 July 2008, 国防工业出版社, pages: 91 * |
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| PB01 | Publication | ||
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| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170118 |
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| RJ01 | Rejection of invention patent application after publication |