CN208829458U - A kind of system for processing chrome-containing wastewater - Google Patents
A kind of system for processing chrome-containing wastewater Download PDFInfo
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- CN208829458U CN208829458U CN201821481836.8U CN201821481836U CN208829458U CN 208829458 U CN208829458 U CN 208829458U CN 201821481836 U CN201821481836 U CN 201821481836U CN 208829458 U CN208829458 U CN 208829458U
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- ceramic membrane
- branch pipe
- containing wastewater
- clear water
- filter tank
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- 239000002351 wastewater Substances 0.000 title claims abstract description 44
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 238000012545 processing Methods 0.000 title claims abstract description 32
- 239000000919 ceramic Substances 0.000 claims abstract description 119
- 239000012528 membrane Substances 0.000 claims abstract description 102
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 56
- 238000006243 chemical reaction Methods 0.000 claims abstract description 28
- 238000010926 purge Methods 0.000 claims description 33
- 238000011001 backwashing Methods 0.000 claims description 19
- 238000011010 flushing procedure Methods 0.000 claims description 11
- 238000005273 aeration Methods 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 8
- 238000005406 washing Methods 0.000 claims description 6
- 238000005192 partition Methods 0.000 claims description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- 229910052593 corundum Inorganic materials 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 239000011159 matrix material Substances 0.000 claims description 3
- 229910001845 yogo sapphire Inorganic materials 0.000 claims description 3
- 239000002086 nanomaterial Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 20
- 230000008569 process Effects 0.000 abstract description 11
- 230000000149 penetrating effect Effects 0.000 abstract description 2
- 239000011651 chromium Substances 0.000 description 16
- 229910052804 chromium Inorganic materials 0.000 description 14
- 230000000694 effects Effects 0.000 description 12
- VQWFNAGFNGABOH-UHFFFAOYSA-K chromium(iii) hydroxide Chemical group [OH-].[OH-].[OH-].[Cr+3] VQWFNAGFNGABOH-UHFFFAOYSA-K 0.000 description 10
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical compound [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 description 6
- 229910001385 heavy metal Inorganic materials 0.000 description 6
- 230000004907 flux Effects 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 4
- 229910000000 metal hydroxide Inorganic materials 0.000 description 4
- 150000004692 metal hydroxides Chemical class 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 238000009388 chemical precipitation Methods 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 230000004044 response Effects 0.000 description 3
- 239000013049 sediment Substances 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000004411 aluminium Substances 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 150000001845 chromium compounds Chemical class 0.000 description 2
- 230000001112 coagulating effect Effects 0.000 description 2
- 230000003750 conditioning effect Effects 0.000 description 2
- QDOXWKRWXJOMAK-UHFFFAOYSA-N dichromium trioxide Chemical compound O=[Cr]O[Cr]=O QDOXWKRWXJOMAK-UHFFFAOYSA-N 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 229910052738 indium Inorganic materials 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 229920002401 polyacrylamide Polymers 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- VEMKTZHHVJILDY-UHFFFAOYSA-N resmethrin Chemical compound CC1(C)C(C=C(C)C)C1C(=O)OCC1=COC(CC=2C=CC=CC=2)=C1 VEMKTZHHVJILDY-UHFFFAOYSA-N 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000000967 suction filtration Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002114 nanocomposite Substances 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- -1 reaction tank Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- HRZFUMHJMZEROT-UHFFFAOYSA-L sodium disulfite Chemical compound [Na+].[Na+].[O-]S(=O)S([O-])(=O)=O HRZFUMHJMZEROT-UHFFFAOYSA-L 0.000 description 1
- 235000010262 sodium metabisulphite Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of system for processing chrome-containing wastewater, it is characterized in that, including reaction tank, ceramic membrane filter tank and clear water reserviors, intake pump and water inlet manifold are connected between the reaction tank and the ceramic membrane filter tank, ceramic membrane with the setting of multiple parallel intervals in the ceramic membrane filter tank, the ceramic membrane have multiple apopores for penetrating through setting along its length, the apopore it is closed at one end, the other end is connected with collection branch pipe；Outfall sewer is connected between the ceramic membrane filter tank and the clear water reserviors, the collection branch pipe is connected to the outfall sewer；Suction pump is provided on the outfall sewer.The advantages that the utility model has occupied area small, and process flow is short, convenient operation and management, stable structure, long service life.
Description
Technical field
The utility model relates to field of environment engineering technology, in particular to a kind of system for processing chrome-containing wastewater.
Background technique
Chromium and compound is industrially widely used, metallurgy, chemical industry, mineral engineering, be electroplated, chromium processed, pigment, pharmacy,
A series of industries such as the production of industry light industry textile industry, chromic salts and chromium compounds, can all generate a large amount of chromate waste water.Wherein, the chemical combination of chromium
Object is mainly with trivalent (such as Cr2O3) and sexavalence (such as CrO4 2-Or Cr2O7 2-) form exist, and toxicity is then most strong with Cr VI, about
It is 100 times of trivalent chromium.
Chemical precipitation method is mainly used to the processing method of chromate waste water at present, process flow is as shown in Figure 1, this method
Take continuous reaction process, first acid adding adjusts the pH value of chromate waste water raw water to acidity into the first pH conditioning tank；Then it will give up
Water flows into reduction pond, by adding reducing agent for hexavalent chrome reduction into trivalent chromium into reduction pond；Waste water subsequently flows into second
PH conditioning tank, then pH value is adjusted to alkalinity to Chi Zhongjia alkali；Waste water flows into coagulating basin again, by the way that polymerization chlorine is added into coagulating basin
Changing aluminium (PAC) and polyacrylamide (PAM) makes chromium hydroxide form wadding body that is biggish, being easy to precipitate；Then in slow water
Enter inclined-tube sedimentation tank under the conditions of stream, using the hydroxide of gravity precipitating chromium, supernatant then flows into sandfiltration pot, by stone
Sand discharges after further filtering.As it can be seen that existing chromate waste water processing chemical precipitation method mainly has following deficiency: using continuous
In different processing units reaction chemically or physically occurs for formula reaction, waste water, but due to the continuity of reaction, is difficult to allow each
Processing unit is all run under optimum condition, and especially when influent quality fluctuates, the variation of water quality is difficult to run through
Change response parameter to respond rapidly to, so that treatment effect be made to fluctuate, or even causes processing not up to standard；It is main to utilize chemistry side
Method forms sediment progress physics settleability to be influenced by reaction condition, change of water quality, even occurs not precipitate or precipitate sometimes
Difficult phenomenon causes to discharge exceeded containing chromium compound with waste water outlet；It is precipitated using inclined-tube sedimentation tank, on inclined tube easily
Fouling causes inclined tube to collapse after long-play, is damaged；For the settleability of the hydroxide of guarantee chromium, reduces and discharge exceeded wind
Danger, often excessive dosing, to generate a large amount of heavy metal sewage sludge precipitating, dangerous waste cost of disposal is high；Process flow is long, takes up an area face
Product is big, and operational administrative is complex.The enterprises such as the plating for generation chromate waste water, due to lacking professional technician, because of people
The phenomenon for causing processing not up to standard for fault is more frequent.
Utility model content
In view of the above shortcomings of the prior art, it is accounted for the technical problem to be solved by the utility model is to how to provide one kind
Ground area is small, and process flow is short, convenient operation and management, stable structure, system for processing chrome-containing wastewater with long service life.
In order to solve the above-mentioned technical problem, the utility model uses the following technical solution:
A kind of system for processing chrome-containing wastewater, which is characterized in that described including reaction tank, ceramic membrane filter tank and clear water reserviors
It is connected with intake pump and water inlet manifold between reaction tank and the ceramic membrane filter tank, has in the ceramic membrane filter tank multiple
The ceramic membrane of parallel interval setting, the ceramic membrane have multiple apopores for penetrating through setting along its length, institute
The closed at one end of apopore is stated, the other end is connected with collection branch pipe；It is connected between the ceramic membrane filter tank and the clear water reserviors
Outfall sewer, the collection branch pipe are connected to the outfall sewer；Suction pump is provided on the outfall sewer.
Using the above structure, waste water to be processed can be put into reaction tank, the pretreatment of waste water is completed in reaction tank,
Metal hydroxides molecule is formed, is then pumped into ceramic membrane filter tank by intake pump, is aspirated by suction pump, make to put down
Negative pressure is formed in the apopore of plate ceramic membrane, pretreated waste water enters in apopore by the filtering of ceramic membrane,
Molecule in waste water, which is blocked, to be retained in ceramic membrane filter tank, and filtered clear water is sent into storage in clear water reserviors, completes to contain
The processing of chromium waste water.Above structure only needs reaction tank, ceramic membrane filter tank and clear water reserviors, and occupied area is small, and process flow is short, behaviour
Make convenient for management.In addition, being filtered using ceramic membrane, it is easy to settle it is not necessary that heavy metal substance to be processed to be processed into
Bulky grain, reduce pretreated difficulty, improve pretreatment efficiency.And the stable structure of ceramic membrane, service life
Long, recycling rate of waterused is higher.
It further, further include the backwashing pump being arranged in parallel with the suction pump, the backwashing pump passes through backwash
Pipe is respectively connected to the outfall sewer and the clear water reserviors, and the water discharging direction of the backwashing pump is towards the collection branch pipe；
The side of the suction pump and backwashing pump towards the collection branch pipe is each provided with a solenoid valve.
Ceramic membrane is backwashed in this way, can use the clear water that backwashing pump extracts in clear water reserviors, makes to adhere to
It falls off in the sediment of flat ceramic film surface, the filter opening of ceramic membrane is avoided to be blocked, influence filter effect and filtering effect
Rate extends the service life of ceramic membrane.The on-off of branch where can control suction pump or backwashing pump by solenoid valve,
Prevent crossfire.
Further, it is additionally provided in the ceramic membrane filter tank and washes away dress for wash away the flat ceramic film surface
It sets.
In this way, washing away using surface of the flusher to ceramic membrane, chromium hydroxide molecule can be prevented
Object deposits on the surface of ceramic membrane, is conducive to extend the service life of ceramic membrane.
Further, the flushing device include in aeration head of the matrix arrangements below the ceramic membrane, and
The air pump being connected on the aeration head.
In this way, can be aerated while suction filtration, so that chromium hydroxide finely ground particles are in aerating gas
Under souring, it can not be attached to the surface of ceramic membrane, the filter opening of ceramic membrane is avoided to block, be conducive to improve plate
The service life of ceramic membrane.
Further, the flushing device includes the air purge branch pipe being arranged between the two neighboring ceramic membrane,
Multiple gas holes being arranged towards the ceramic membrane are provided on the air purge branch pipe, the air purge branch pipe is total by air purge
Pipe is connected to compressor.
In this way, passing through the air purge branch pipe being arranged between two neighboring ceramic membrane using the pressure-air of compressor
High pressure washing is carried out to flat ceramic film surface, can will be partially depositing in the chromium hydroxide molecule of flat ceramic film surface
Object rinses out, and without rinsing assembling after dismantling ceramic membrane, extends the maintenance period of ceramic membrane, improves use
Service life.
Further, the air purge branch pipe is arranged along the length direction of the ceramic membrane, and along the flat ceramic
The width direction of film is evenly equipped with multiple.
In this way, high pressure gas can be made to rinse the whole surface for covering ceramic membrane, making for ceramic membrane is improved
Use the service life.
Further, flowmeter is additionally provided on the outfall sewer.
In this way, can control effluent flux, system is made to operate in optimum state.
Further, pressure gauge is additionally provided on the outfall sewer.
Further, the ceramic membrane uses Al2O3Nano material is made, the surface distribution of the ceramic membrane
Having aperture is 0.5~1.0 μm of filtering aperture.
Further, also there is the run-off being separated to form with partition, the height of the partition is lower than in the clear water reserviors
The depth of the clear water reserviors；The water outlet of the outfall sewer is connected to the run-off.
In this way, filtered clear water can be made further to precipitate in run-off, and the clear water on upper layer is made to flow into clear water reserviors
In, be conducive to the effect for further increasing processing.
In conclusion the utility model has occupied area small, process flow is short, convenient operation and management, and stable structure makes
With the service life it is long the advantages that.
Detailed description of the invention
Fig. 1 is existing process for processing chromate-containing waste water flow chart.
Fig. 2 is the structural schematic diagram of the system for processing chrome-containing wastewater of the application.
Fig. 3 is the air purge general pipeline of flushing device and the structural schematic diagram of air purge branch pipe in Fig. 2.
Fig. 4 is the position relationship structural diagram of air purge branch pipe and ceramic membrane.
Specific embodiment
Below with reference to embodiment, the utility model is described in further detail.
When specific implementation: as shown in Figure 2 to 4, a kind of system for processing chrome-containing wastewater, including reaction tank, ceramic membrane filter tank 2
And clear water reserviors 8, intake pump and water inlet manifold, the pottery are connected between the reaction tank and the ceramic membrane filter tank 2
Ceramic membrane 3 with the setting of multiple parallel intervals in porcelain membrane filtration pond 2, the ceramic membrane 3 have multiple along length side
To perforation setting apopore, the apopore it is closed at one end, the other end is connected with collection branch pipe 4；The ceramic membrane filter tank 2
Outfall sewer 5 is connected between the clear water reserviors 8, the collection branch pipe 4 is connected to the outfall sewer 5；The water outlet
Suction pump 6 is provided on general pipeline 5.
Using the above structure, waste water to be processed can be put into reaction tank, the pretreatment of waste water is completed in reaction tank,
Metal hydroxides molecule is formed, is then pumped into ceramic membrane filter tank by intake pump, is aspirated by suction pump, make to put down
Negative pressure is formed in the apopore of plate ceramic membrane, pretreated waste water enters in apopore by the filtering of ceramic membrane,
Molecule in waste water, which is blocked, to be retained in ceramic membrane filter tank, and filtered clear water is sent into storage in clear water reserviors, completes to contain
The processing of chromium waste water.Above structure only needs reaction tank, ceramic membrane filter tank and clear water reserviors, and occupied area is small, and process flow is short, behaviour
Make convenient for management.In addition, being filtered using ceramic membrane, it is easy to settle it is not necessary that heavy metal substance to be processed to be processed into
Bulky grain, reduce pretreated difficulty, improve pretreatment efficiency.And the stable structure of ceramic membrane, service life
Long, recycling rate of waterused is higher.
It further include the backwashing pump 7 being arranged in parallel with the suction pump 6 when implementation, the backwashing pump 7 passes through backwash
Pipe is respectively connected to the outfall sewer 5 and the clear water reserviors 8, branch of catchmenting described in the water discharging direction direction of the backwashing pump 7
Pipe 4；The side of the suction pump 6 and backwashing pump 7 towards the collection branch pipe 4 is each provided with a solenoid valve.
Ceramic membrane is backwashed in this way, can use the clear water that backwashing pump extracts in clear water reserviors, makes to adhere to
It falls off in the sediment of flat ceramic film surface, the filter opening of ceramic membrane is avoided to be blocked, influence filter effect and filtering effect
Rate extends the service life of ceramic membrane.The on-off of branch where can control suction pump or backwashing pump by solenoid valve,
Prevent crossfire.
When implementation, the flushing device for washing away 3 surface of ceramic membrane is additionally provided in the ceramic membrane filter tank 2
10。
In this way, washing away using surface of the flusher to ceramic membrane, chromium hydroxide molecule can be prevented
Object deposits on the surface of ceramic membrane, is conducive to extend the service life of ceramic membrane.
When implementation, the flushing device 10 include in aeration head of the matrix arrangements below the ceramic membrane 3, and
The air pump being connected on the aeration head.
In this way, can be aerated while suction filtration, so that chromium hydroxide finely ground particles are in aerating gas
Under souring, it can not be attached to the surface of ceramic membrane, the filter opening of ceramic membrane is avoided to block, be conducive to improve plate
The service life of ceramic membrane.
When implementation, the flushing device 10 includes the air purge branch pipe being arranged between the two neighboring ceramic membrane 3
11, multiple gas holes 12 being arranged towards the ceramic membrane 3, the air purge branch pipe 11 are provided on the air purge branch pipe 11
Compressor is connected to by air purge general pipeline 13.
In this way, passing through the air purge branch pipe being arranged between two neighboring ceramic membrane using the pressure-air of compressor
High pressure washing is carried out to flat ceramic film surface, can will be partially depositing in the chromium hydroxide molecule of flat ceramic film surface
Object rinses out, and without rinsing assembling after dismantling ceramic membrane, extends the maintenance period of ceramic membrane, improves use
Service life.
The air purge branch pipe is arranged along the length direction of the ceramic membrane 3, and along the width of the ceramic membrane 3
Direction is evenly equipped with multiple；In this way, high pressure gas can be made to rinse the whole surface for covering ceramic membrane, flat ceramic is improved
The service life of film.Gas hole on each air purge branch pipe is evenly equipped with multiple groups, and gas hole described in every group along its length
The gas hole being uniformly arranged including four along the circumferential direction of the air purge branch pipe；In this way, can make full use of between ceramic membrane
Gap, using an air purge branch pipe can simultaneously the flat ceramic film surface of two sides is rinsed.Each air blowing
The direction in hole and the angle of the ceramic membrane 3 are 45 degree；In this way, blowing direction is made to blow to flat ceramic along 45 degree of angles
Film enables gas to form tangential active force in ceramic membrane surface, micro- to the chromium hydroxide for peeling off ceramic membrane surface deposition
Small particle flushing effect is more preferable.The gas hole on the two neighboring air purge branch pipe is along the length side of the air purge branch pipe
To shifting to install；In this way, can prevent the air-flow of the gas hole on two neighboring air purge branch pipe from interfering with each other, it is adjacent convenient for shortening
The spacing of two air purge branch pipes enables the gas hole on air purge branch pipe to blow to the plate in the region of adjacent air purge branch pipe institute face
Ceramic membrane surface, flushing effect is more preferably.Further, the flat ceramic film surface also has along the air purge branch pipe length direction
Face is arranged one by one for the arc groove of setting, the arc groove and the air purge branch pipe.In this way, being set in flat ceramic film surface
Arc groove is set, the surface area of ceramic membrane can be increased, so that filter area is bigger.The air scour of gas hole is to arc
After in groove, it arcuately can form eddy flow by groove, stir the liquid of flat ceramic film surface, effectively prevent the hydroxide washed out
Chromium finely ground particles deposit again.
When implementation, flowmeter is additionally provided on the outfall sewer 5.
In this way, can control effluent flux, system is made to operate in optimum state.
When implementation, pressure gauge is additionally provided on the outfall sewer 5.
The ceramic membrane uses micropore size to be made of 0.5 ~ 1.0 μm of nanocomposite, described nano combined
Material is by Al2O3、ZrO2And TiO2Nanoparticle synthesizes under 1600 C high temperature.
Also there is the run-off 9 being separated to form with partition, the height of the partition is lower than the clear water in the clear water reserviors 8
The depth in pond；The water outlet of the outfall sewer 5 is connected to the run-off 9.
In this way, filtered clear water can be made further to precipitate in run-off, and the clear water on upper layer is made to flow into clear water reserviors
In, be conducive to the effect for further increasing processing.
When specific processing, using following steps:
First waste water is flowed into reaction tank, and adds dilute sulfuric acid into reaction tank, between adjusting pH value to 2 ~ 3, after stablizing
Sodium pyrosulfite is added again, makes its oxidation reduction potential control in 250mV hereinafter, controlling the reaction time simultaneously not less than 30min；
After the reaction was completed, adding NaOH thereto rises to pH value between 8 ~ 9, and pre-reaction is completed after stablizing.It can also be to reaction tank
In continue to add micro aluminium polychloride (PAC) solution, add ratio be 10 ~ 20mg/l, to promote metal hydroxides small
The formation of particle.Stirrer paddle is arranged in pond in pre-reaction, it is ensured that reaction carries out complete.Entire pre-reaction time is 1 ~ 1.5h.
Waste water is pumped into ceramic membrane filter tank again, starting suction pump is aspirated, and the operating pressure for controlling suction pump is less than
30kPa, effluent flux are 40 ~ 60L/(m2H), prevent plane ceramic film from quickly blocking；Suction of the waste water in ceramic membrane filter tank
Time is 1.5 ~ 2.0h.
Wash away the surface of ceramic membrane by air pump continuous aeration in aspiration procedure to prevent chromium hydroxide small
Grain object deposits on the surface of ceramic membrane, and the air pump can be blower or air compressor.Control aeration volume flow is every
10 ~ 15 times of hour processing water.For example, 1h handles 10m3Waste water, the then aeration quantity during handling should be 100 ~ 150m3。
Meanwhile in aspiration procedure, at interval of 5 minutes, stop suction 1 minute, and be pumped into air purge general pipeline using compressor
Pressure-air is sprayed by the gas hole on air purge branch pipe towards flat ceramic film surface, is blown in the generation of flat ceramic film surface
Effect is swept, the deposit stripping of flat ceramic film surface will be accumulated in.It is 1Mpa that compressed air, which designs stripping pressure,.
It is filtered water outlet enter clear water reserviors in, periodically from clear water reserviors extract clear water to ceramic membrane recoil with
Restore membrane flux, backwashing period 2h, back washing strength is 80 ~ 100L/(m2H), backwashing time≤5min.
After each filtration treatment end cycle, chromium-bearing sludge is discharged, the sludge quantity that discharge period visual response generates determines, most
It is usually no more than for 24 hours greatly.
Compared with conventional processes, above-mentioned treatment process is had the advantages that
1, fuzzy operation (each processing unit is difficult to all the reach optimum condition) defect of successive reaction bring is solved, is precisely controlled
The response parameter of each link is made, realizes optimal conditions operation, it is ensured that the efficiency and effect of reaction.
2, chromium hydroxide will be contained using other modes to separate from system, and will avoid chemical precipitation effect is unstable from showing
As.
3, (under same flow condition, the heavy metal sewage sludge of generation only has tradition to the yield of the reduction sludge of hydroxide containing chromium
The 1/3 ~ 1/2 of the precipitation method), reduce dangerous waste cost of disposal.Also, as total chromium concn >=1000mg/l in waste water, due to dirt
Coagulated agent is free of in mud, there is higher purity, the economy with heavy metal recovery.
4, simplify processing links, system is made to be physically easier to perform management；Solution metal hydroxides accumulates on inclined tube to be caused
Collapse the problem of, reduce the complexity and cost of system maintenance.
5, (being discharged total chromium concn can be in 0.1mg/l hereinafter, far below country's mark for stably reaching standard discharge after ensuring wastewater treatment
Quasi- 1.0mg/l).
Meanwhile with it is some using the technique of flat ceramic film process heavy metal wastewater thereby compared with, duplex film that the present invention uses
Pollution control measures can effectively remove the pollutant of film surface attachment, maintain membrane flux.The pulse air laid along membrane surface
The more thick and heavy pollutant for being deposited on film surface is broken up or is removed film surface by the high-intensitive compressed air that pipe generates, and is backwashed
Water further washes out residual deposit.And stronger back washing strength is used, is cleaned more thorough.
The above is only the preferred embodiment of the utility model only, is not limitation with the utility model, all at this
Made any modifications, equivalent replacements, and improvements etc., should be included in the utility model within the spirit and principle of utility model
Protection scope within.
Claims (10)
1. a kind of system for processing chrome-containing wastewater, which is characterized in that including reaction tank (1), ceramic membrane filter tank (2) and clear water reserviors
(8), intake pump and water inlet manifold, the ceramic membrane are connected between the reaction tank (1) and the ceramic membrane filter tank (2)
Ceramic membrane (3) with the setting of multiple parallel intervals in filter tank (2), the ceramic membrane (3) have multiple along length
Direction perforation setting apopore, the apopore it is closed at one end, the other end is connected with collection branch pipe (4)；The ceramic membrane
It is connected between filter tank (2) and the clear water reserviors (8) outfall sewer (5), it is total that the collection branch pipe (4) is connected to the water outlet
It manages (5)；Suction pump (6) are provided on the outfall sewer (5).
2. system for processing chrome-containing wastewater as described in claim 1, which is characterized in that further include in parallel with the suction pump (6)
The backwashing pump (7) of setting, the backwashing pump (7) are respectively connected to the outfall sewer (5) and described by backwash tube
Clear water reserviors (8), the water discharging direction of the backwashing pump (7) is towards the collection branch pipe (4)；The suction pump (6) and backwash
The side of pump (7) towards the collection branch pipe (4) is each provided with a solenoid valve.
3. system for processing chrome-containing wastewater as described in claim 1, which is characterized in that also set up in the ceramic membrane filter tank (2)
There is the flushing device (10) for washing away the ceramic membrane (3) surface.
4. system for processing chrome-containing wastewater as claimed in claim 3, which is characterized in that the flushing device (10) includes in matrix
The aeration head being arranged in below the ceramic membrane (3), and the air pump being connected on the aeration head.
5. system for processing chrome-containing wastewater as claimed in claim 3, which is characterized in that the flushing device (10) includes that setting exists
Air purge branch pipe between the two neighboring ceramic membrane (3) is provided on the air purge branch pipe multiple towards the plate
The gas hole of ceramic membrane (3) setting, the air purge branch pipe are connected to compressor by air purge general pipeline.
6. system for processing chrome-containing wastewater as claimed in claim 5, which is characterized in that the air purge branch pipe is along the flat ceramic
The length direction of film (3) is arranged, and is evenly equipped with along the width direction of the ceramic membrane (3) multiple.
7. system for processing chrome-containing wastewater as described in claim 1, which is characterized in that be additionally provided on the outfall sewer (5)
Flowmeter.
8. system for processing chrome-containing wastewater as described in claim 1, which is characterized in that be additionally provided on the outfall sewer (5)
Pressure gauge.
9. system for processing chrome-containing wastewater as described in claim 1, which is characterized in that the ceramic membrane (3) uses Al2O3
Nano material is made, and the filtering aperture that aperture is 0.5~1.0 μm is distributed in the surface of the ceramic membrane (3).
10. system for processing chrome-containing wastewater as described in claim 1, which is characterized in that also have in the clear water reserviors (8) with every
The run-off (9) that plate is separated to form, the height of the partition are lower than the depth of the clear water reserviors (8)；The outfall sewer (5)
Water outlet is connected to the run-off (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821481836.8U CN208829458U (en) | 2018-09-11 | 2018-09-11 | A kind of system for processing chrome-containing wastewater |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821481836.8U CN208829458U (en) | 2018-09-11 | 2018-09-11 | A kind of system for processing chrome-containing wastewater |
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| Publication Number | Publication Date |
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| CN208829458U true CN208829458U (en) | 2019-05-07 |
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| CN201821481836.8U Expired - Fee Related CN208829458U (en) | 2018-09-11 | 2018-09-11 | A kind of system for processing chrome-containing wastewater |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108821481A (en) * | 2018-09-11 | 2018-11-16 | 重庆亚领环保科技有限公司 | A kind of system for processing chrome-containing wastewater and processing method |
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2018
- 2018-09-11 CN CN201821481836.8U patent/CN208829458U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108821481A (en) * | 2018-09-11 | 2018-11-16 | 重庆亚领环保科技有限公司 | A kind of system for processing chrome-containing wastewater and processing method |
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