CN108017232A - It is biodegradable to quantify test method with the in-situ synchronization of absorbing synergic efficiency - Google Patents
It is biodegradable to quantify test method with the in-situ synchronization of absorbing synergic efficiency Download PDFInfo
- Publication number
- CN108017232A CN108017232A CN201711287436.3A CN201711287436A CN108017232A CN 108017232 A CN108017232 A CN 108017232A CN 201711287436 A CN201711287436 A CN 201711287436A CN 108017232 A CN108017232 A CN 108017232A
- Authority
- CN
- China
- Prior art keywords
- water
- column
- bridging
- activated carbon
- water treatment
- 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
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 29
- 238000010998 test method Methods 0.000 title claims abstract description 26
- 230000002195 synergetic effect Effects 0.000 title claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 318
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 196
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 claims abstract description 56
- 238000001179 sorption measurement Methods 0.000 claims abstract description 54
- 239000007788 liquid Substances 0.000 claims abstract description 42
- 238000000034 method Methods 0.000 claims abstract description 31
- 238000000855 fermentation Methods 0.000 claims abstract description 30
- 230000004151 fermentation Effects 0.000 claims abstract description 30
- 238000011068 loading method Methods 0.000 claims abstract description 30
- 150000001875 compounds Chemical class 0.000 claims abstract description 23
- 230000001580 bacterial effect Effects 0.000 claims abstract description 19
- 238000006065 biodegradation reaction Methods 0.000 claims abstract description 17
- 238000010521 absorption reaction Methods 0.000 claims description 81
- 230000001105 regulatory effect Effects 0.000 claims description 52
- 241000894006 Bacteria Species 0.000 claims description 47
- 238000005273 aeration Methods 0.000 claims description 37
- 230000001954 sterilising effect Effects 0.000 claims description 34
- 238000004659 sterilization and disinfection Methods 0.000 claims description 34
- 229910052799 carbon Inorganic materials 0.000 claims description 33
- 239000003610 charcoal Substances 0.000 claims description 31
- 238000011001 backwashing Methods 0.000 claims description 28
- 239000005416 organic matter Substances 0.000 claims description 20
- 238000013329 compounding Methods 0.000 claims description 18
- 238000009825 accumulation Methods 0.000 claims description 16
- 238000009826 distribution Methods 0.000 claims description 14
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 12
- 230000005540 biological transmission Effects 0.000 claims description 12
- 238000011010 flushing procedure Methods 0.000 claims description 9
- 238000012545 processing Methods 0.000 claims description 9
- OSVXSBDYLRYLIG-UHFFFAOYSA-N chlorine dioxide Inorganic materials O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 claims description 8
- 238000005276 aerator Methods 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 230000001276 controlling effect Effects 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 4
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 4
- 238000005070 sampling Methods 0.000 claims description 4
- 239000006004 Quartz sand Substances 0.000 claims description 3
- 239000001963 growth medium Substances 0.000 claims description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 2
- 239000000523 sample Substances 0.000 claims description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 239000000126 substance Substances 0.000 claims 1
- 238000011160 research Methods 0.000 description 7
- 239000003651 drinking water Substances 0.000 description 6
- 235000020188 drinking water Nutrition 0.000 description 6
- 238000013139 quantization Methods 0.000 description 6
- 239000005446 dissolved organic matter Substances 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 238000011835 investigation Methods 0.000 description 2
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 230000001360 synchronised effect Effects 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 231100001239 persistent pollutant Toxicity 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 230000008054 signal transmission Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000005728 strengthening 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
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
- C02F1/325—Irradiation devices or lamp constructions
-
- 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
- C02F2003/001—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
- C02F2003/003—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms using activated carbon or the like
-
- 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
- C02F2303/04—Disinfection
-
- 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
- C02F2303/16—Regeneration of sorbents, filters
-
- 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
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Biological Treatment Of Waste Water (AREA)
- Water Treatment By Sorption (AREA)
- Physical Water Treatments (AREA)
Abstract
Biodegradable to quantify test method with the in-situ synchronization of absorbing synergic efficiency, the present invention relates to a kind of water treatment test method, it cooperates with efficiency to be difficult to quantify to solve the problems, such as to adsorb in Bioaugnentation activated carbon process with biodegradation.Quantify test method：First, compound functional bacterial liquid carries out aerated fermentation in barrel shape fermentation tank, and the compound functional bacterial liquid for completion of fermenting enters U-shaped bridging Bioaugnentation active carbon water treatment apparatus and carries out repeated loading；2nd, raw water it is sterilized and pretreatment after respectively enter in U-shaped bridging Bioaugnentation active carbon water treatment apparatus and U-shaped bridging activated carbon adsorption water treatment facilities；3rd, the accumulative removal amount of content of organics and the accumulative removal amount of U-shaped bridging activated carbon adsorption water treatment facilities content of organics in U-shaped bridging Bioaugnentation active carbon water treatment apparatus Inlet and outlet water are contrasted.The water treatment test method of the present invention can be realized to the biodegradable in-situ synchronization quantitatively evaluating that efficiency is cooperateed with activated carbon adsorption under diversified operational mode.
Description
Technical field
The present invention relates to a kind of water treatment test method, and in particular to a kind of biodegradable original position with absorbing synergic efficiency
It is synchronous to quantify test method, belong to Advanced Treatment of Drinking Water and field of scientific study.
Background technology
To tackle increasingly serious pollution of waterhead, water supply quality quality is improved, cities and towns drinking water safety is ensured, with activated carbon
Widely promoted for the Advanced Treatment of Drinking Water of core.Wherein, with Bioaugnentation activated carbon (Bio-enhanced
Activated Carbon-BEAC) technology be core drinking water advanced treatment technique, organically combined the efficient suction of activated carbon
Attached effect and the biodegradation of the stability and high efficiency of preponderant functional bacteria.Suction-operated and the combination of biodegradation are not
It can only realize and complicated natural and persistent pollutant in micro-polluted source water is effectively removed, while activated carbon surface can be promoted
The bio-regeneration of absorption point position, effectively extends the replacement cycle of activated carbon, reduces water producing cost.
By the further investigation and popularization and application of nearly more than 20 years, Bioaugnentation Advanced Treatment Process with Activated Carbon reached its maturity,
It is increasingly becoming a kind of ripe, stable and dynamical advanced treatment process.Engineer application and a large amount of basic research confirm, living
Property charcoal absorption and the biodegradable synergistic effect of preponderant functional bacteria be leading machine that BEAC techniques remove dissolubility pollutant in water removal
Reason.Absorption and the biodegradable performance for cooperate with efficiency are to promote activated carbon surface to adsorb the key for putting position in-situ regeneration, right
There are extremely important influence in BEAC performance efficiencies and activated carbon service life.Therefore, by cooperateing with effect with biodegradation for absorption
The research of energy, proposes effective regulation and control method, to effectively improving performance efficiency, reducing operating cost, guarantee drinking water safety tool
There are important promotion meaning and application value.
But at present, BEAC absorption and the mechanism that influences each other of biodegradation, and conspiracy relation between the two is still
It is unintelligible, scientific and reasonable research method is not yet formed, particularly in-situ synchronization quantization method.Therefore, it is biodegradable with adsorbing
The in-situ synchronization quantization method for cooperateing with efficiency is the key scientific problems urgently illustrated.The above-mentioned science of scientific and reasonable solution
Problem, by ensureing that Drinking Water in China water supply security has important science, application value with promoting meaning.In addition, it is applied to
Absorption cooperates with the globality research method of efficiency and experimental rig still still to belong to empty with biodegradation in research BAC process
In vain.
The content of the invention
The purpose of the present invention is to solve absorption in Bioaugnentation activated carbon process to cooperate with efficiency to be difficult to biodegradation
The problem of carrying out in-situ synchronization quantization, and then a kind of biodegradable and absorbing synergic efficiency in-situ synchronization is provided and quantifies to test
Method.
The in-situ synchronization of biodegradation of the invention and absorbing synergic efficiency quantifies test method and follows these steps to realize：
First, compound functional bacterial liquid and culture medium are added in barrel shape fermentation tank, setting fermentation temperature and opening temperature reality
When measuring and controlling, aerated fermentation is then carried out into barrel shape fermentation tank by micro-hole aerator, reaches predetermined fermentation time
Afterwards, ferment completion compound functional bacterial liquid by zymocyte liquid delivery pipe be delivered to bacterium solution compounding and repeated loading water tank in, bacterium
Compound functional bacterial liquid in liquid compounding and repeated loading water tank pressurizes through bacterium solution circulating pump is delivered to U-shaped bridge through bacterium solution circulation pipe
Even in the pressure pre-column of Bioaugnentation active carbon water treatment apparatus, the solenoid valve on the first bridging pipe, compound functional bacteria are opened
Liquid pass sequentially through it is active-carbon bed in active-carbon bed, the first bridging pipe and pressure post column in pressure pre-column, then from position
Water outlet at the top of pressure post column is back in bacterium solution compounding and repeated loading water tank by return duct, completes compound work(
The repeated loading of energy bacterium solution；
The wherein described U-shaped bridging Bioaugnentation active carbon water treatment apparatus is led to by pressure pre-column and pressure post column
The the first bridging pipe for crossing bottom is connected, and solenoid valve is provided with the first bridging pipe, in pressure pre-column and pressure post column
Be respectively arranged with it is active-carbon bed, the pressure pre-column of U-shaped bridging Bioaugnentation active carbon water treatment apparatus and pressure post column
Bottom is respectively arranged with the first backwash tube and the second backwash tube；
2nd, the ultraviolet sterilization component in ultraviolet sterilization raw water regulating tank is opened, raw water is led to after the pressurization of raw water pulsating pump
Cross raw water suction hose to flow into ultraviolet sterilization raw water regulating tank, the raw water after sterilization treatment passes through raw water pipelined
To barrel shape aeration water quality regulating device, the ultraviolet lamp module in barrel shape aeration water quality regulating device is opened, it is pre- in barrel shape aeration water quality regulating device
Processing raw water passes through U-shaped bridging Bioaugnentation by middle transmission ＆ distribution pipeline and active carbon water treatment apparatus water inlet pipe in sinking
It is active-carbon bed in the pressure pre-column of active carbon water treatment apparatus, pass through pressure postposition by the first bridging Guan Houcheng upper up-flows
It is active-carbon bed in column, clear water is delivered to through No.1 clear water feed-line by the water outlet at the top of pressure post column after processing
In case；
Meanwhile the pretreatment raw water in barrel shape aeration water quality regulating device enters U-shaped bridge by middle transmission ＆ distribution pipeline in sinking
The absorption activated carbon bed of pre-column is even adsorbed in activated carbon adsorption water treatment facilities, passes through suction in upper up-flow through the second bridging pipe
The absorption activated carbon bed of attached post column, the water after adsorption treatment is by adsorbing the water outlet at the top of post column through clear water delivery pipe
Line is delivered in filtered water tank；
The wherein described U-shaped bridging activated carbon adsorption water treatment facilities is to pass through bottom by absorption pre-column and absorption post column
The second bridging pipe in portion is connected, and solenoid valve is provided with the second bridging pipe, in absorption pre-column and absorption post column respectively
It is provided with absorption activated carbon bed, the absorption pre-column of U-shaped bridging activated carbon adsorption water treatment facilities and the bottom for adsorbing post column
It is respectively arranged with the 3rd backwash tube and the 4th backwash tube；
3rd, respectively to U-shaped bridging Bioaugnentation active carbon water treatment apparatus and U-shaped bridging activated carbon adsorption water treatment facilities
Inlet and outlet water water quality index be detected, content of organics is tired in the Inlet and outlet water of U-shaped bridging activated carbon adsorption water treatment facilities
Product removal amount is quantified as the organic matter accumulation adsorbance Q that suction-operated is contributedAd, U-shaped bridging Bioaugnentation activated carbon water process
The accumulative removal amount Q of content of organics in device Inlet and outlet waterComSubtract what U-shaped bridging activated carbon adsorption water treatment facilities was contributed
Organic matter accumulation adsorbance QAd, remaining organic matter accumulative removal amount is U-shaped bridging Bioaugnentation active carbon water treatment apparatus
The biodegradable amount Q of organic matter accumulation that middle function bacterium biodegradation is contributedBio；
When U-shaped bridging Bioaugnentation active carbon water treatment apparatus and the head of U-shaped bridging activated carbon adsorption water treatment facilities
When loss and water quality reach backwashing period, the backwashing water in filtered water tank irradiates by ultraviolet lamp module and comes from ClO2Hair
ClO prepared by raw device2After combined disinfection sterilizing, the backwashing water in filtered water tank is by backwashing suction hose through backwash pump
After pressurization, U-shaped bridging Bioaugnentation active carbon water treatment apparatus is separately flowed into by the first backwash tube and the second backwash tube
Pressure pre-column and pressure post column, close the first bridging pipe on solenoid valve, in pressure pre-column and pressure post column
It is active-carbon bed backwashed, flushing water is discharged by water outlet at the top of pressure pre-column and pressure post column；
Backwashing water in filtered water tank separately flows into U-shaped bridging activated carbon by the 3rd backwash tube and the 4th backwash tube
The absorption pre-column and absorption post column of water treatment facilities are adsorbed, the solenoid valve on the second bridging pipe is closed, to adsorbing pre-column
It is rinsed with the absorption activated carbon bed in absorption post column, flushing water is by adsorbing at the top of pre-column and absorption post column
Water outlet is discharged, and completes the anti-of bridging Bioaugnentation active carbon water treatment apparatus and U-shaped bridging activated carbon adsorption water treatment facilities
Rinse.
The present invention is after each backwashing period, with dissolved organic matter (DOC), total organic carbon (TOC) or height
Mangaic acid salt index (CODMn) it is basic index, realize that U-shaped bridging Bioaugnentation activated carbon water process fills by following calculation
Put the middle biodegradable quantitatively evaluating process with suction-operated to organic pollutant removal ability.In quantizing process, U-shaped bridging
Content of organics (DOC, TOC or COD in the Inlet and outlet water of activated carbon adsorption water treatment facilitiesMn) accumulative removal amount can be quantified as
Organic matter that suction-operated is contributed accumulation adsorbance, it is organic in U-shaped bridging Bioaugnentation active carbon water treatment apparatus Inlet and outlet water
Thing content (DOC, TOC or CODMn) accumulative removal amount subtract U-shaped bridging activated carbon adsorption water treatment facilities contributed it is organic
Thing accumulates adsorbance, and remaining organic matter accumulative removal amount is function in U-shaped bridging Bioaugnentation active carbon water treatment apparatus
The biodegradable amount of organic matter accumulation that bacterium biodegradation is contributed.
The in-situ synchronization of biodegradation of the invention and absorbing synergic efficiency quantifies test method and has the advantages that：
1st, present invention firstly provides it is a kind of it is biodegradable quantify test method with the in-situ synchronization of absorbing synergic efficiency, can be with
The organic matter accumulation clearly contributed function bacterium biodegradation in Bioaugnentation activated carbon process system is biodegradable
Amount；
2nd, it is proposed by the present invention it is a kind of it is biodegradable quantify test method with the in-situ synchronization of absorbing synergic efficiency, can be with
Instruct water treatment plant to select the absorbent charcoal carrier of economical and efficient, build the Bioaugnentation activated carbon process system of efficient stable；
3rd, water treatment test method proposed by the present invention can be realized to the Bioaugnentation activity under diversified operational mode
The biodegradable in-situ synchronization quantitatively evaluating that efficiency is cooperateed with activated carbon adsorption in charcoal process system；
4th, also it is drink while the present invention provides a kind of new U-shaped bridging Bioaugnentation activated carbon advanced treatment apparatus
The basis in the field such as Related Mechanism and performance efficiency reinforcing is handled with water depth and engineering Application Research provides effective experiment
Method.
Brief description of the drawings
Fig. 1 is the biodegradation in embodiment one and the in-situ synchronization quantization experimental rig of absorbing synergic efficiency
Structure diagram.
Embodiment
Embodiment one：Present embodiment is biodegradable to quantify test method with the in-situ synchronization of absorbing synergic efficiency
Follow these steps to implement：
First, compound functional bacterial liquid and culture medium are added in barrel shape fermentation tank A-1, setting fermentation temperature and opening temperature
Real-time measuring and controlling, then carries out aerated fermentation into barrel shape fermentation tank A-1 by micro-hole aerator A-1-1, reaches pre-
After determining fermentation time, the compound functional bacterial liquid for completion of fermenting is delivered to bacterium solution compounding and repeated loading by zymocyte liquid delivery pipe
In water tank A-2, bacterium solution compounding and repeated loading water tank A-2 in compound functional bacterial liquid through bacterium solution circulating pump A-2-2 pressurize through bacterium
Liquid circulation pipe A-2-1 is delivered in the pressure pre-column D-1 of U-shaped bridging Bioaugnentation active carbon water treatment apparatus D, opens the
Solenoid valve on one bridging pipe D-3, compound functional bacterial liquid pass sequentially through active-carbon bed D-4 in pressure pre-column D-1, first
Active-carbon bed D-4 in bridging pipe D-3 and pressure post column D-2, then from the water outlet at the top of pressure post column D-2
It is back to by return duct 6 in bacterium solution compounding and repeated loading water tank A-2, completes the repeated loading of compound functional bacterial liquid；
The wherein described U-shaped bridging Bioaugnentation active carbon water treatment apparatus D is by pressure pre-column D-1 and pressure postposition
Column D-2 is connected by the first bridging pipe D-3 of bottom, solenoid valve is provided with the first bridging pipe D-3, in pressure pre-column
Active-carbon bed D-4 is respectively arranged with D-1 and pressure post column D-2, U-shaped bridging Bioaugnentation active carbon water treatment apparatus D's
The bottom of pressure pre-column D-1 and pressure post column D-2 are respectively arranged with the first backwash tube 7 and the second backwash tube 8；
2nd, the ultraviolet sterilization component B-2-1 in ultraviolet sterilization raw water regulating tank B-2 is opened, raw water is through raw water pulsating pump
Flowed into after B-1 pressurizations by raw water suction hose B-3 in ultraviolet sterilization raw water regulating tank B-2, the raw water after sterilization treatment passes through
Raw water pipeline 1 is delivered to barrel shape aeration water quality regulating device C-1, opens the ultraviolet lamp module in barrel shape aeration water quality regulating device C-1
Pretreatment raw water in C-1-2, barrel shape aeration water quality regulating device C-1 by middle transmission ＆ distribution pipeline 4 and active carbon water treatment apparatus into
Water pipe 5 is in active-carbon bed D- in the pressure pre-column D-1 that sinking passes through U-shaped bridging Bioaugnentation active carbon water treatment apparatus D
4, pressure is passed through after processing by the active-carbon bed D-4 in pressure post column D-2 in upper up-flow after the first bridging pipe D-3
Water outlet at the top of post column D-2 is delivered in filtered water tank F-1 through No.1 clear water feed-line 14；
Meanwhile the pretreatment raw water in barrel shape aeration water quality regulating device C-1 enters U by middle transmission ＆ distribution pipeline 4 in sinking
The absorption activated carbon bed E-4 of pre-column E-1 is adsorbed in type bridging activated carbon adsorption water treatment facilities E, through the second bridging pipe E-3
In upper up-flow by adsorbing the absorption activated carbon bed E-4 of post column E-2, the water after adsorption treatment is by adsorbing post column E-2 tops
The water outlet in portion is delivered in filtered water tank F-1 through clear water feed-line 15；
The wherein described U-shaped bridging activated carbon adsorption water treatment facilities E is by absorption pre-column E-1 and absorption post column E-
2 are connected by the second bridging pipe E-3 of bottom, and solenoid valve is provided with the second bridging pipe E-3, in absorption pre-column E-1
Absorption activated carbon bed E-4, the suction of U-shaped bridging activated carbon adsorption water treatment facilities E are respectively arranged with absorption post column E-2
The bottom of attached pre-column E-1 and absorption post column E-2 are respectively arranged with the 3rd backwash tube 9 and the 4th backwash tube 10；
3rd, U-shaped bridging Bioaugnentation active carbon water treatment apparatus D and U-shaped bridging activated carbon adsorption water process are filled respectively
The Inlet and outlet water water quality index for putting E is detected, content of organics in the Inlet and outlet water of U-shaped bridging activated carbon adsorption water treatment facilities E
Accumulative removal amount be quantified as the organic matter accumulation adsorbance Q that suction-operated contributedAd, U-shaped bridging Bioaugnentation activated carbon water
The accumulative removal amount Q of content of organics in processing unit D Inlet and outlet watersComSubtract U-shaped bridging activated carbon adsorption water treatment facilities E institutes
The organic matter accumulation adsorbance Q of contributionAd, remaining organic matter accumulative removal amount is at U-shaped bridging Bioaugnentation activated carbon water
The biodegradable amount Q of organic matter accumulation that function bacterium biodegradation is contributed in reason device DBio；
As U-shaped bridging Bioaugnentation active carbon water treatment apparatus D and the water of U-shaped bridging activated carbon adsorption water treatment facilities E
When head loss and water quality reach backwashing period, the backwashing water in filtered water tank F-1 is irradiated and come by ultraviolet lamp module F-1-1
From ClO2ClO prepared by generator G-22After combined disinfection sterilizing, the backwashing water in filtered water tank F-1 is by backwashing suction hose
2 after backwash pump F-2 pressurizations, and separately flowing into U-shaped bridging biology by the first backwash tube 7 and the second backwash tube 8 increases
The pressure pre-column D-1 and pressure post column D-2 of strongly active charcoal water treatment facilities D, closes the electromagnetism on the first bridging pipe D-3
Valve, backwashes the active-carbon bed D-4 in pressure pre-column D-1 and pressure post column D-2, before flushing water is by pressure
Put the water outlet discharge at the top of column D-1 and pressure post column D-2；
Backwashing water in filtered water tank F-1 separately flows into U-shaped bridging by the 3rd backwash tube 9 and the 4th backwash tube 10
The absorption pre-column E-1 and absorption post column E-2 of activated carbon adsorption water treatment facilities E, closes the electricity on the second bridging pipe E-3
Magnet valve, is rinsed the absorption activated carbon bed E-4 in absorption pre-column E-1 and absorption post column E-2, flushing water passes through suction
Water outlet discharge at the top of attached pre-column E-1 and absorption post column E-2, completes bridging Bioaugnentation active carbon water treatment apparatus D
With the backwash of U-shaped bridging activated carbon adsorption water treatment facilities E.
Present embodiment is biodegradable to include function bacterium fermentation with the in-situ synchronization of absorbing synergic efficiency quantization experimental rig
And repeated loading device A, raw water and sterilization device B, preposition pretreatment unit C, U-shaped bridging Bioaugnentation activated carbon
Water treatment facilities D, U-shaped bridging activated carbon adsorption water treatment facilities E, back purge system F and Study on influencing factors auxiliary equipment G；
The wherein described function bacterium fermentation and repeated loading device A include barrel shape fermentation tank A-1, bacterium solution compounding and circulation
Water tank A-2 and aeration pump A-3 is loaded, the tank bottom of barrel shape fermentation tank A-1 is provided with micro-hole aerator A-1-1, barrel shape fermentation tank
A-1 is compounded by zymocyte liquid delivery pipe with bacterium solution and repeated loading water tank A-2 is connected, and is set in zymocyte liquid delivery pipe
Zymocyte liquid delivery pump A-1-2 is equipped with, liquid outlet and bacterium solution circulation pipe positioned at bacterium solution compounding and repeated loading water tank A-2 bottoms
A-2-1 is connected, and bacterium solution circulating pump A-2-2, aeration pump A-3 are provided with bacterium solution circulation pipe A-2-1 and passes through aeration tube and micropore
Aerator A-1-1 is connected；
The raw water and sterilization device B include raw water pulsating pump B-1 and ultraviolet sterilization raw water regulating tank B-
2, raw water suction hose B-3 are connected with the water inlet of ultraviolet sterilization raw water regulating tank B-2, are set in raw water suction hose B-3
There is raw water pulsating pump B-1, the axial direction in ultraviolet sterilization raw water regulating tank B-2 is provided with multiple ultraviolet sterilization component B-2-1,
One end of raw water pipeline 1 is connected with the water outlet of ultraviolet sterilization raw water regulating tank B-2, is set in raw water pipeline 1
It is equipped with raw water force (forcing) pump B-5；
The preposition pretreatment unit C includes barrel shape aeration water quality regulating device C-1 and intermediate lift pump C-2, raw water
The other end of pipeline 1 is connected with the water inlet of barrel shape aeration water quality regulating device C-1, is set in the bottom of barrel shape aeration water quality regulating device C-1
Ozone diffuser C-1-1 is equipped with, ozone diffuser C-1-1 is connected with one end of ozone feed-line 3, in barrel shape water quality adjustment
Axially disposed in device C-1 to have multiple ultraviolet lamp module C-1-2, one end and the barrel shape water quality adjustment of middle transmission ＆ distribution pipeline 4 fill
The bottom water outlet for putting C-1 is connected, and intermediate lift pump C-2 is provided with middle transmission ＆ distribution pipeline 4；
The U-shaped bridging Bioaugnentation active carbon water treatment apparatus D is by pressure pre-column D-1 and pressure post column D-
2 are connected by the first bridging pipe D-3 of bottom, solenoid valve are provided with the first bridging pipe D-3, in pressure pre-column D-1
Be respectively arranged with active-carbon bed D-4 in pressure post column D-2, the other end and the pressure pre-column D- of bacterium solution circulation pipe A-2-1
1 water inlet is connected, and one end of active carbon water treatment apparatus water inlet pipe 5 is connected with bacterium solution circulation pipe A-2-1, activated carbon water
The other end of processing unit water inlet pipe 5 is connected with middle transmission ＆ distribution pipeline 4, and the water outlet at the top of pressure post column D-2 leads to
The refluxing opening for crossing return duct 6 and bacterium solution compounding and repeated loading water tank A-2 is connected, the top delivery port of pressure post column D-2 with
One end of No.1 clear water feed-line 14 is connected；
The U-shaped bridging activated carbon adsorption water treatment facilities E is led to by absorption pre-column E-1 and absorption post column E-2
The the second bridging pipe E-3 for crossing bottom is connected, and solenoid valve is provided with the second bridging pipe E-3, in absorption pre-column E-1 and suction
Absorption activated carbon bed E-4, the other end and the absorption pre-column E-1 of middle transmission ＆ distribution pipeline 4 are respectively arranged with attached post column E-2
The water inlet at top is connected；Absorption post column E-2 top delivery ports are connected with one end of No. two clear water feed-lines 15；
The back purge system F includes filtered water tank F-1 and backwash pump F-2, axially disposed in filtered water tank F-1
There are multiple ultraviolet lamp component F-1-1, the other end of No.1 clear water feed-line 14 and the water inlet of filtered water tank F-1 left upper portions
It is connected, the other end of No. two clear water feed-lines 15 is connected with the water inlet of filtered water tank F-1 right upper portions, and backwash is inhaled
One end of water pipe 2 is connected with the bottom of filtered water tank F-1, in the pressure of U-shaped bridging Bioaugnentation active carbon water treatment apparatus D
The bottom of pre-column D-1 and pressure post column D-2 are respectively arranged with the first backwash tube 7 and the second backwash tube 8, in U type bridges
Even it is anti-to be respectively arranged with the 3rd for the bottom of the absorption pre-column E-1 of activated carbon adsorption water treatment facilities E and absorption post column E-2
9 and the 4th backwash tube 10 of flush pipe, the first backwash tube 7 and the second backwash tube 8 are in parallel and with backwashing suction hose 2
It is connected, the 3rd backwash tube 9 and the 4th backwash tube 10 are in parallel and are connected with backwash suction hose 2, are inhaled in backwash
Backwash pump F-2 is provided with water pipe 2；
The Study on influencing factors auxiliary equipment G includes ozone generating-device G-1, ClO2Generator G-2 and water quality tune
Regulating device G-3, filtered water tank F-1 pass through No. three inlet tubes 13 and No.1 inlet tube 11 and ClO2Generator G-2 is connected, ozone
The other end of feed-line 3 is connected with ozone generating-device G-1, ClO2The outlet of generator G-2 and the one of No.1 inlet tube 11
End is connected, and the other end of No.1 inlet tube 11 is connected with the inlet of barrel shape aeration water quality regulating device C-1, aeration water quality regulating device
G-3 is connected by No. two inlet tubes 12 with the inlet positioned at barrel shape aeration water quality regulating device C-1 bottoms.
The structure that the in-situ synchronization of biodegradation and absorbing synergic efficiency described in present embodiment quantifies experimental rig is shown
It is intended to as shown in Figure 1, being provided with liquid level linkage liquid level gauge A-4, bacterium solution circulation in bacterium solution compounding and repeated loading water tank A-2
The start and stop of A-2-2 are pumped by liquid level linkage liquid level gauge A-4 coordinated signals.Liquid is provided with ultraviolet sterilization raw water regulating tank B-2
Position linkage liquid level gauge, liquid level linkage liquid level gauge and raw water pulsating pump B-1 and raw water force (forcing) pump B-5 coordinated signals.In filtered water tank
Liquid level gauge F-3, liquid level gauge F-3 and backwash pump F-2 coordinated signals are provided with F-1.
The structure of present embodiment ultraviolet sterilization component is to install ultraviolet lamp tube additional in quartz socket tube, as needed with branched
Fluorescent tube is that one group of form makes ultraviolet module.
The raw water and sterilization device of present embodiment can be connected directly to U-shaped bridging life by raw water pipeline
Thing strengthens the top water inlet pipe of activated carbon pressure pre-column, realizes and preposition pretreatment unit is surmounted.
Present embodiment barrel shape fermentation tank, bacterium solution compounding and repeated loading water tank, ultraviolet sterilization raw water regulating device, barrel shape
Aeration water quality regulating device, U-shaped bridging Bioaugnentation activated carbon pressure pre-column, U-shaped bridging Bioaugnentation activated carbon pressure postposition
The material of column, U-shaped bridging activated carbon adsorption pre-column and U-shaped bridging activated carbon adsorption post column is organic glass or stainless
Steel.
Embodiment two：The present embodiment is different from the first embodiment in that in barrel shape aeration water quality regulating device C-
Ozone diffuser C-1-1 is provided with 1, ozone diffuser C-1-1 passes through ozone feed-line 3 and ozone generating-device G-1 phases
Even.Other steps and parameter are identical with embodiment one.
Embodiment three：The present embodiment is different from the first and the second embodiment in that aeration water quality regulating device G-3
It is connected by No. two inlet tubes 12 with barrel shape aeration water quality regulating device C-1.Other steps and parameter and embodiment one or
Two is identical.
Embodiment four：Present embodiment is filled from aeration water quality regulating device G-3 unlike embodiment three
There are liquor natrii hypochloritis or hydrogen peroxide solution.Other steps and parameter are identical with embodiment three.
Embodiment five：In barrel shape water quality tune unlike one of present embodiment and embodiment one to four
Quartz sand filter media is provided with regulating device C-1.Other steps and parameter are identical with one of embodiment one to four.
Present embodiment can realize synchronous investigation sand filtration pair by loading quartz sand filter media in barrel shape aeration water quality regulating device
Subsequent bio strengthens the influence of activated carbon process and active carbon absorption technology water purification efficiency.
Embodiment six：Pressure pre-column D- unlike one of present embodiment and embodiment one to five
Active-carbon bed D-4 in 1 and pressure post column D-2 loads broken charcoal, briquetting charcoal, column charcoal or ball-type charcoal, absorption pre-column E-
Absorption activated carbon bed E-4 in 1 and absorption post column E-2 loads broken charcoal, briquetting charcoal, column charcoal or ball-type charcoal.Other steps
Rapid and parameter is identical with one of embodiment one to five.
The activated carbon loaded in the active-carbon bed bed with absorption activated carbon of present embodiment is identical.
Present embodiment passes through in pressure pre-column D-1 and pressure post column D-2, absorption pre-column E-1 and absorption postposition
Broken charcoal, briquetting charcoal, column charcoal or ball-type charcoal are loaded in column E-2, can be realized to different type activated carbon structure feature to net
The influencing mechanism research of water efficiency, selects the activated carbon of more appropriate source water quality characteristic.
Embodiment seven：Given birth to unlike one of present embodiment and embodiment one to six in U-shaped bridging
Water sampling pipe is provided with the side wall of thing enhancing active carbon water treatment apparatus D, in U-shaped bridging activated carbon adsorption water treatment facilities E
Side wall on be also provided with water sampling pipe.Other steps and parameter are identical with one of embodiment one to six.
Embodiment eight：In barrel shape fermentation tank unlike one of present embodiment and embodiment one to seven
A-1, bacterium solution compounding and repeated loading water tank A-2, ultraviolet sterilization raw water regulating tank B-2, barrel shape aeration water quality regulating device C-1, U
Wireless biography is both provided with type bridging Bioaugnentation active carbon water treatment apparatus D, U-shaped bridging activated carbon adsorption water treatment facilities E
Water delivery matter is popped one's head in.Other steps and parameter are identical with one of embodiment one to seven.
Present embodiment will be wirelessly transferred water quality probe and carry out signal transmission with monitoring and cloud data sharing device, with to water
Matter index monitors in real time.
Embodiment nine：Circulated in step 1 unlike one of present embodiment and embodiment one to eight
For loading process using circulation 4h, the mode of interval 2h is a cycle.Other steps and parameter and embodiment one to eight
One of it is identical.
Embodiment ten：It is anti-in step 3 unlike one of present embodiment and embodiment one to nine
Flushing cycle is 8~12 days.Other steps and parameter are identical with one of embodiment one to nine.
Embodiment：The present embodiment is biodegradable to be followed these steps with the in-situ synchronization of absorbing synergic efficiency quantization test method
Realize：
The first, 1L is derived to the compound work(in the ozone-biological active carbon filter tank of urban water supply factory stable operation on charcoal
Can bacterium solution be added in barrel shape fermentation tank A-1, add 20~30L nutrient solutions, set fermentation temperature as in the range of 15 DEG C~20 DEG C
And the real-time measuring and controlling of opening temperature, then it is aerated by micro-hole aerator A-1-1 into barrel shape fermentation tank A-1
Ferment 24h, and after reaching predetermined fermentation time, the compound functional bacterial liquid for completion of fermenting is delivered to bacterium by zymocyte liquid delivery pipe
Liquid compound and repeated loading water tank A-2 in, bacterium solution compounding and repeated loading water tank A-2 in compound functional bacterial liquid followed through bacterium solution
Before ring pump A-2-2 pressurizations are delivered to the pressure of U-shaped bridging Bioaugnentation active carbon water treatment apparatus D through bacterium solution circulation pipe A-2-1
Put in column D-1, open the solenoid valve on the first bridging pipe D-3, compound functional bacterial liquid is passed sequentially through in pressure pre-column D-1
Active-carbon bed D-4 in active-carbon bed D-4, the first bridging pipe D-3 and pressure post column D-2, is then flowed back by return duct 6
To bacterium solution compounding and repeated loading water tank A-2, the repeated loading of compound functional bacterial liquid is completed, after the completion of repeated loading, is closed
Solenoid valve on barrel shape fermentation tank A-1, aeration pump A-3 and zymocyte liquid delivery pump A-1-2 and pipeline, repeated loading process are adopted
With circulation 4h, interval 2h is a cycle, carries out 4 cycles altogether；
The wherein described U-shaped bridging Bioaugnentation active carbon water treatment apparatus D is by pressure pre-column D-1 and pressure postposition
Column D-2 is connected by the first bridging pipe D-3 of bottom, solenoid valve is provided with the first bridging pipe D-3, in pressure pre-column
Active-carbon bed D-4 is respectively arranged with D-1 and pressure post column D-2；
2nd, the ultraviolet sterilization component B-2-1 in ultraviolet sterilization raw water regulating tank B-2, the work(of each ultraviolet lamp tube are opened
Rate is set as 40W, and the Song Hua River source water (water quality index sees attached list 1) after coagulation-depositing technology processing is through raw water pulsating pump
By raw water suction hose B-3 with 0.2m after B-1 pressurizations3The flow velocity of/h is flowed into ultraviolet sterilization raw water regulating tank B-2, waterpower
Residence time is 20min, and the raw water after sterilization treatment is by raw water pipeline 1 with 0.2m3The flow velocity of/h is delivered to barrel shape water
Matter regulating device C-1, the ultraviolet lamp module C-1-2 opened in barrel shape aeration water quality regulating device C-1 are sterilized again, are passed through
After the pretreatment of 20min, pretreatment raw water is by middle transmission ＆ distribution pipeline 4 and active carbon water treatment apparatus water inlet pipe 5 with 0.1 m3/
The flow velocity of h is in active-carbon bed in pressure pre-column D-1 of the sinking by U-shaped bridging Bioaugnentation active carbon water treatment apparatus D
D-4, passes through the active-carbon bed D-4 in pressure post column D-2, U-shaped bridging biology after the first bridging pipe D-3 in upper up-flow
The overall air-land combat for strengthening active carbon water treatment apparatus D is 25min, U-shaped bridging Bioaugnentation activated carbon water process dress
The active-carbon bed D-4 put in D uses coal quality briquetting crushing activated carbon, its leading indicator is：Specific surface area SBET=1214m2/ g,
Total hole volume V=1.013cm3/ g, mechanical strength ＞ 90%, grain size distribution are 8 × 30 mesh, pass through pressure post column after processing
Water outlet at the top of D-2 is delivered in filtered water tank F-1 through No.1 clear water feed-line 14；
Meanwhile the pretreatment raw water in barrel shape aeration water quality regulating device C-1 passes through middle transmission ＆ distribution pipeline 4 with 0.1m3The stream of/h
Speed enters in U-shaped bridging activated carbon adsorption water treatment facilities E the absorption activated carbon bed E-4 for adsorbing pre-column E-1 in sinking,
Through the second bridging pipe E-3 in upper up-flow by adsorbing the absorption activated carbon bed E-4 of post column E-2, U-shaped bridging activated carbon adsorption
The overall air-land combat of water treatment facilities E is 25min, the activated carbon in U-shaped bridging activated carbon adsorption water treatment facilities E
Bed E-4 uses coal quality briquetting crushing activated carbon, its leading indicator is：Specific surface area SBET=1214m2/ g, total hole volume V=
1.013cm3/ g, mechanical strength ＞ 90%, grain size distribution are 8 × 30 mesh, and the water after adsorption treatment is by adsorbing post column E-2
The water outlet at top is delivered in filtered water tank F-1 through No. two clear water feed-lines 15；
The wherein described U-shaped bridging activated carbon adsorption water treatment facilities E is by absorption pre-column E-1 and absorption post column E-
2 are connected by the second bridging pipe E-3 of bottom, and solenoid valve is provided with the second bridging pipe E-3, in absorption pre-column E-1
Absorption activated carbon bed E-4 is respectively arranged with absorption post column E-2；
3rd, the water of U-shaped bridging Bioaugnentation active carbon water treatment apparatus D and U-shaped bridging activated carbon adsorption water treatment facilities E
Head loss and water quality is when reaching backwashing period, and backwashing period is 10d in the present embodiment, the backwashing water in filtered water tank F-1
Irradiated by ultraviolet lamp module F-1-1 (power of each ultraviolet lamp tube is 30W) and come from ClO2ClO prepared by generator G-22
After (equivalent effective chlorine 1.0mg/L) combined disinfection sterilizing, the backwashing water in filtered water tank F-1 is by backwashing suction hose 2 through anti-
After flush water pump F-2 pressurizations, U-shaped bridging Bioaugnentation is separately flowed into by the first backwash tube 7 and the second backwash tube 8 and is lived
Property charcoal water treatment facilities D pressure pre-column D-1 and pressure post column D-2, close the solenoid valve on the first bridging pipe D-3, it is right
Active-carbon bed D-4 in pressure pre-column D-1 and pressure post column D-2 is backwashed, and flushing water passes through pressure pre-column D-
The backwashing time of water outlet discharge at the top of 1 and pressure post column D-2, pressure pre-column D-1 and pressure post column D-2 are equal
For 10min, the expansion rate of charcoal bed D-4 is kept to control 50% or so；
Meanwhile by ultraviolet lamp component F-1-1, (power of each ultraviolet lamp tube is the backwashing water in filtered water tank F-1
30W) irradiation is with coming from ClO2ClO prepared by generator G-22After (equivalent effective chlorine 1.0mg/L) combined disinfection sterilizing, filtered water tank
Backwashing water in F-1 is anti-by the 3rd backwash tube 9 and the 4th by backwashing suction hose 2 after backwash pump pressurizes
Flush pipe 10 separately flows into the absorption pre-column E-1 and absorption post column E-2 of U-shaped bridging activated carbon adsorption water treatment facilities E,
The solenoid valve on the second bridging pipe E-3 is closed, to absorption pre-column E-1 and adsorbs the absorption activated carbon bed E- in post column E-2
4 are rinsed, and flushing water is discharged by the water outlet for adsorbing pre-column E-1 and adsorbing at the top of post column E-2, adsorbs pre-column
The backwashing time of E-1 and absorption post column E-2 are 10min, keep the expansion rate control of charcoal bed E-4 50% or so, complete
Into the backwash of bridging Bioaugnentation active carbon water treatment apparatus D and U-shaped bridging activated carbon adsorption water treatment facilities E；
After each backwashing period, close backwash pump F-2 and backwash suction hose 2, first backwashes
Solenoid valve on 7 and second backwash tube 8 of pipe, the 3rd backwash tube 9 and the 4th backwash tube 10, and opened again from step 2
Begin to operate.
Periodically to U-shaped bridging Bioaugnentation active carbon water treatment apparatus D and U-shaped bridging activated carbon adsorption water treatment facilities E
Inlet and outlet water water quality index be detected, choose permanganate index (CODMn) it is basic index, it is real to pass through following calculation
Biodegradable and suction-operated is to organic pollutant removal ability in existing U-shaped bridging Bioaugnentation active carbon water treatment apparatus D
Quantitatively evaluating process；In quantizing process, content of organics in the Inlet and outlet water of U-shaped bridging activated carbon adsorption water treatment facilities E
(CODMn) accumulative removal amount can be quantified as the organic matter accumulation adsorbance Q that suction-operated contributedAd(mg/kg), U types bridging
Content of organics (COD in Bioaugnentation active carbon water treatment apparatus D Inlet and outlet watersMn) accumulative removal amount QCom(mg/kg) U is subtracted
The organic matter accumulation adsorbance Q that type bridging activated carbon adsorption water treatment facilities E is contributedAd(mg/kg), remaining organic matter tires out
Product removal amount be in U-shaped bridging Bioaugnentation active carbon water treatment apparatus D function bacterium biodegradation contributed it is organic
The biodegradable amount Q of thing accumulationBio(mg/kg)；U-shaped bridging biology increases during continuous operation being calculated in the present embodiment 200 days
Organic matter biodegradable and that absorption is contributed adds up the variation tendency of removal amount, specific number in strongly active charcoal water treatment facilities D
According to for details see attached table shown in 2；It can be seen from Table 2 that it can be embodied based on the embodiment of the present invention raw in the different operation phase
Absorption and biodegradable quantitative relationship in thing enhancing activated carbon process, solve the problem that bioprocess is difficult to synchronously quantify.
Subordinate list 1：The main water quality index of water inlet of embodiment sewerage disposing device D and water treatment facilities E
Subordinate list 2：The quantitative relationship of adsorbance and the biodegradable amount of accumulation is accumulated in water treatment facilities E
Claims (10)
1. biodegradable quantify test method with the in-situ synchronization of absorbing synergic efficiency, it is characterised in that this method is by following step
It is rapid to realize：
First, compound functional bacterial liquid and culture medium are added in barrel shape fermentation tank (A-1), setting fermentation temperature and opening temperature reality
When measuring and controlling, then reached by micro-hole aerator (A-1-1) to aerated fermentation is carried out in barrel shape fermentation tank (A-1)
After predetermined fermentation time, the compound functional bacterial liquid for completion of fermenting is delivered to bacterium solution compounding by zymocyte liquid delivery pipe and circulation is negative
Carry in water tank (A-2), the compound functional bacterial liquid in bacterium solution compounding and repeated loading water tank (A-2) is through bacterium solution circulating pump (A-2-2)
Pressurization is delivered to the pressure pre-column of U-shaped bridging Bioaugnentation active carbon water treatment apparatus (D) through bacterium solution circulation pipe (A-2-1)
(D-1) in, the solenoid valve on the first bridging pipe (D-3) is opened, compound functional bacterial liquid is passed sequentially through in pressure pre-column (D-1)
Active-carbon bed (D-4) in active-carbon bed (D-4), the first bridging pipe (D-3) and pressure post column (D-2), then from positioned at pressure
Water outlet at the top of power post column (D-2) is back in bacterium solution compounding and repeated loading water tank (A-2) by return duct (6), complete
Into the repeated loading of compound functional bacterial liquid；
The wherein described U-shaped bridging Bioaugnentation active carbon water treatment apparatus (D) is by pressure pre-column (D-1) and pressure postposition
Column (D-2) is connected by the first bridging pipe (D-3) of bottom, solenoid valve is provided with the first bridging pipe (D-3), before pressure
Put in column (D-1) and pressure post column (D-2) and be respectively arranged with active-carbon bed (D-4), at U-shaped bridging Bioaugnentation activated carbon water
Reason device (D) pressure pre-column (D-1) and pressure post column (D-2) bottom be respectively arranged with the first backwash tube (7) and
Second backwash tube (8)；
2nd, the ultraviolet sterilization component (B-2-1) in ultraviolet sterilization raw water regulating tank (B-2) is opened, raw water is through raw water pulsating pump
(B-1) flowed into after pressurizeing by raw water suction hose (B-3) in ultraviolet sterilization raw water regulating tank (B-2), the original after sterilization treatment
Water is delivered to barrel shape aeration water quality regulating device (C-1) by raw water pipeline (1), opens in barrel shape aeration water quality regulating device (C-1)
Ultraviolet lamp module (C-1-2), pretreatment raw water in barrel shape aeration water quality regulating device (C-1) by middle transmission ＆ distribution pipeline (4) and
Active carbon water treatment apparatus water inlet pipe (5) is in pressure of the sinking by U-shaped bridging Bioaugnentation active carbon water treatment apparatus (D)
It is active-carbon bed (D-4) in pre-column (D-1), pass through after the first bridging pipe (D-3) in upper up-flow in pressure post column (D-2)
Active-carbon bed (D-4), it is defeated through No.1 clear water feed-line (14) by the water outlet at the top of pressure post column (D-2) after processing
Send into filtered water tank (F-1)；
Meanwhile the pretreatment raw water in barrel shape aeration water quality regulating device (C-1) enters U by middle transmission ＆ distribution pipeline (4) in sinking
The absorption activated carbon bed (E-4) of absorption pre-column (E-1) in type bridging activated carbon adsorption water treatment facilities (E), through the second bridging
For pipe (E-3) in upper up-flow by adsorbing the absorption activated carbon bed (E-4) of post column (E-2), the water after adsorption treatment passes through absorption
Water outlet at the top of post column (E-2) is delivered in filtered water tank (F-1) through clear water feed-line (15)；
The wherein described U-shaped bridging activated carbon adsorption water treatment facilities (E) is by absorption pre-column (E-1) and absorption post column
(E-2) it is connected by the second bridging pipe (E-3) of bottom, solenoid valve is provided with the second bridging pipe (E-3), it is preposition adsorbing
Absorption activated carbon bed (E-4), U-shaped bridging activated carbon adsorption water process are respectively arranged with column (E-1) and absorption post column (E-2)
The bottom of the absorption pre-column (E-1) of device (E) and absorption post column (E-2) is respectively arranged with the 3rd backwash tube (9) and the
Four backwash tubes (10)；
3rd, respectively to U-shaped bridging Bioaugnentation active carbon water treatment apparatus (D) and U-shaped bridging activated carbon adsorption water treatment facilities
(E) Inlet and outlet water water quality index is detected, and the disengaging Organic substance in water of U-shaped bridging activated carbon adsorption water treatment facilities (E) contains
The accumulative removal amount of amount is quantified as the organic matter accumulation adsorbance Q that suction-operated is contributedAd, U-shaped bridging Bioaugnentation activated carbon
The accumulative removal amount Q of content of organics in water treatment facilities (D) Inlet and outlet waterComSubtract U-shaped bridging activated carbon adsorption water treatment facilities
(E) the organic matter accumulation adsorbance Q contributedAd, remaining organic matter accumulative removal amount is U-shaped bridging Bioaugnentation activated carbon
The biodegradable amount Q of organic matter accumulation that function bacterium biodegradation is contributed in water treatment facilities (D)Bio；
When the water of U-shaped bridging Bioaugnentation active carbon water treatment apparatus (D) and U-shaped bridging activated carbon adsorption water treatment facilities (E)
When head loss and water quality reach backwashing period, the backwashing water in filtered water tank (F-1) is irradiated by ultraviolet lamp module (F-1-1)
With from ClO2ClO prepared by generator (G-2)2After combined disinfection sterilizing, the backwashing water in filtered water tank (F-1) passes through recoil
Suction hose (2) is washed after backwash pump (F-2) pressurization, is flowed respectively by the first backwash tube (7) and the second backwash tube (8)
Enter the pressure pre-column (D-1) and pressure post column (D-2) of U-shaped bridging Bioaugnentation active carbon water treatment apparatus (D), close the
Solenoid valve on one bridging pipe (D-3), to active-carbon bed (D-4) in pressure pre-column (D-1) and pressure post column (D-2) into
Row backwash, flushing water are discharged by the water outlet at the top of pressure pre-column (D-1) and pressure post column (D-2)；
Backwashing water in filtered water tank (F-1) separately flows into U-shaped bridge by the 3rd backwash tube (9) and the 4th backwash tube (10)
Even the absorption pre-column (E-1) of activated carbon adsorption water treatment facilities (E) and absorption post column (E-2), close the second bridging pipe (E-
3) solenoid valve on, is rinsed the absorption activated carbon bed (E-4) in absorption pre-column (E-1) and absorption post column (E-2),
Flushing water is discharged by the water outlet for adsorbing pre-column (E-1) and adsorbing at the top of post column (E-2), is completed bridging Bioaugnentation and is lived
Property charcoal water treatment facilities (D) and the backwash of U-shaped bridging activated carbon adsorption water treatment facilities (E).
2. biodegradable and absorbing synergic efficiency in-situ synchronization according to claim 1 quantifies test method, its feature
It is to be provided with ozone diffuser (C-1-1) in barrel shape aeration water quality regulating device (C-1), ozone diffuser (C-1-1) is by smelly
Oxygen feed-line (3) is connected with ozone generating-device (G-1).
3. biodegradable and absorbing synergic efficiency in-situ synchronization according to claim 1 quantifies test method, its feature
It is that aeration water quality regulating device (G-3) is connected by No. two inlet tubes (12) with barrel shape aeration water quality regulating device (C-1).
4. biodegradable and absorbing synergic efficiency in-situ synchronization according to claim 3 quantifies test method, its feature
It is liquor natrii hypochloritis or hydrogen peroxide solution are housed in aeration water quality regulating device (G-3).
5. biodegradable and absorbing synergic efficiency in-situ synchronization according to claim 1 quantifies test method, its feature
It is to be provided with quartz sand filter media in barrel shape aeration water quality regulating device (C-1).
6. biodegradable and absorbing synergic efficiency in-situ synchronization according to claim 1 quantifies test method, its feature
It is that active-carbon bed (D-4) in pressure pre-column (D-1) and pressure post column (D-2) loads broken charcoal, briquetting charcoal, column charcoal
Or ball-type charcoal, absorption pre-column (E-1) and the absorption activated carbon bed (E-4) adsorbed in post column (E-2) load broken charcoal, briquetting
Charcoal, column charcoal or ball-type charcoal.
7. biodegradable and absorbing synergic efficiency in-situ synchronization according to claim 1 quantifies test method, its feature
It is to be provided with water sampling pipe on the side wall of U-shaped bridging Bioaugnentation active carbon water treatment apparatus (D), in U-shaped bridging activity
Water sampling pipe is also provided with the side wall of charcoal absorption water treatment facilities (E).
8. biodegradable and absorbing synergic efficiency in-situ synchronization according to claim 1 quantifies test method, its feature
Be barrel shape fermentation tank (A-1), bacterium solution compounding and repeated loading water tank (A-2), ultraviolet sterilization raw water regulating tank (B-2),
Barrel shape aeration water quality regulating device (C-1), U-shaped bridging Bioaugnentation active carbon water treatment apparatus (D), U-shaped bridging activated carbon adsorption water
It is both provided with processing unit (E) and is wirelessly transferred water quality probe.
9. biodegradable and absorbing synergic efficiency in-situ synchronization according to claim 1 quantifies test method, its feature
In the repeated loading process use circulation 4h in step 1, the mode of interval 2h is a cycle.
10. biodegradable and absorbing synergic efficiency in-situ synchronization according to claim 1 quantifies test method, its feature
It it is 8~12 days in the backwashing period in step 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711287436.3A CN108017232A (en) | 2017-12-07 | 2017-12-07 | It is biodegradable to quantify test method with the in-situ synchronization of absorbing synergic efficiency |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711287436.3A CN108017232A (en) | 2017-12-07 | 2017-12-07 | It is biodegradable to quantify test method with the in-situ synchronization of absorbing synergic efficiency |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108017232A true CN108017232A (en) | 2018-05-11 |
Family
ID=62078727
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711287436.3A Pending CN108017232A (en) | 2017-12-07 | 2017-12-07 | It is biodegradable to quantify test method with the in-situ synchronization of absorbing synergic efficiency |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108017232A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001170672A (en) * | 1999-12-17 | 2001-06-26 | Sumitomo Precision Prod Co Ltd | Waste water treatment method |
| CN1597578A (en) * | 2004-07-22 | 2005-03-23 | 哈尔滨工业大学 | Water treatment method for realizing drinking water deep purification by fixed bioactive carbon technology |
| CN101215072A (en) * | 2008-01-14 | 2008-07-09 | 中国市政工程华北设计研究院 | Biological activated carbon sea water treatment method for increasing organism degradability |
| CN103395952A (en) * | 2013-08-20 | 2013-11-20 | 哈尔滨工业大学 | Water processing apparatus with functions of ozone oxidation, bio-augmentation by tow levels of active carbon and ultraviolet sterilization |
-
2017
- 2017-12-07 CN CN201711287436.3A patent/CN108017232A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001170672A (en) * | 1999-12-17 | 2001-06-26 | Sumitomo Precision Prod Co Ltd | Waste water treatment method |
| CN1597578A (en) * | 2004-07-22 | 2005-03-23 | 哈尔滨工业大学 | Water treatment method for realizing drinking water deep purification by fixed bioactive carbon technology |
| CN101215072A (en) * | 2008-01-14 | 2008-07-09 | 中国市政工程华北设计研究院 | Biological activated carbon sea water treatment method for increasing organism degradability |
| CN103395952A (en) * | 2013-08-20 | 2013-11-20 | 哈尔滨工业大学 | Water processing apparatus with functions of ozone oxidation, bio-augmentation by tow levels of active carbon and ultraviolet sterilization |
Non-Patent Citations (1)
| Title |
|---|
| 张多英等: "O3-BEAC-UV/Cl工艺去除低温水中氨氮的研究", 《中国给水排水》 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102557348B (en) | Soil remediation and sewage purification integrated ecological treatment device | |
| CN103394278B (en) | Method and device for processing ethylene oxide waste gas | |
| US9375663B2 (en) | Sanitization and regeneration of porous filter media with ozone in backwash | |
| US20120318146A1 (en) | Exhaust oxygen recycling apparatus for ozone treatment equipment, and ozone-using system having same | |
| CN101250000A (en) | Advanced treatment method for removing iron-manganese in water | |
| CN204039221U (en) | A kind of biomembrance process four pond purification system of rural domestic sewage treatment | |
| CN109052821A (en) | A kind of the pharmacy wastewater treatment device and its operation method of efficient resource recycling low energy consumption | |
| CN103910467A (en) | Method for processing aquatic product culture waste water | |
| CN101412551A (en) | Enhanced flocculation-hyperfiltration combined process and apparatus for emergency handling of drinking water | |
| CN106007181A (en) | Tidal mixed flow constructed wetland system and sewage treatment method | |
| CN105502838A (en) | Copper-plating waste water purification system and water purification method | |
| CN109205928A (en) | A kind of method and system of advanced treating percolate | |
| CN101177317A (en) | Enhanced compounded mix multi-stage alternate wetland sewage treating process and apparatus thereof | |
| CN201116291Y (en) | Advanced wastewater treatment device | |
| CN104230070B (en) | A kind of method for treating water and system for preparing micromolecular water | |
| CN101045596A (en) | Aeration inner circulation type garbage infiltration liquid two-phase treatment reactor | |
| CN201850194U (en) | Biochemical treatment device for sand filter/ozone/aeration biological filter | |
| CN207451863U (en) | A kind of modularization is layered bio-trickling sewage disposal system | |
| CN207552138U (en) | The biodegradable in-situ synchronization quantization experimental rig with absorbing synergic efficiency | |
| CN108017232A (en) | It is biodegradable to quantify test method with the in-situ synchronization of absorbing synergic efficiency | |
| CN104118938A (en) | A magnetic anaerobic/aerobic biofiltration water purification system and a water purification method | |
| CN206570169U (en) | Water body in lake in-situ purification system | |
| CN1344690A (en) | Water treating method and treater for producing pure health water | |
| RU198738U1 (en) | WATER CLEANER | |
| CN101062819B (en) | Sewage treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180511 |
|
| WD01 | Invention patent application deemed withdrawn after publication |