CN106915863A - A kind of oil refining sewerage biological treatment device - Google Patents
A kind of oil refining sewerage biological treatment device Download PDFInfo
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- CN106915863A CN106915863A CN201510983379.7A CN201510983379A CN106915863A CN 106915863 A CN106915863 A CN 106915863A CN 201510983379 A CN201510983379 A CN 201510983379A CN 106915863 A CN106915863 A CN 106915863A
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- oil refining
- treatment device
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- 238000007670 refining Methods 0.000 title claims abstract description 37
- 230000007062 hydrolysis Effects 0.000 claims abstract description 47
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 47
- 230000020477 pH reduction Effects 0.000 claims abstract description 38
- 238000005273 aeration Methods 0.000 claims abstract description 36
- 239000010802 sludge Substances 0.000 claims abstract description 33
- 239000010865 sewage Substances 0.000 claims abstract description 28
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000000126 substance Substances 0.000 claims abstract description 13
- 238000001556 precipitation Methods 0.000 claims abstract description 10
- 230000008021 deposition Effects 0.000 claims abstract description 7
- 239000013618 particulate matter Substances 0.000 claims abstract description 5
- 230000000630 rising effect Effects 0.000 claims abstract description 3
- 230000003647 oxidation Effects 0.000 claims description 35
- 238000007254 oxidation reaction Methods 0.000 claims description 35
- 239000000945 filler Substances 0.000 claims description 17
- 238000006243 chemical reaction Methods 0.000 claims description 16
- 229920002635 polyurethane Polymers 0.000 claims description 16
- 239000004814 polyurethane Substances 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 238000004065 wastewater treatment Methods 0.000 claims description 4
- 230000001186 cumulative effect Effects 0.000 claims description 2
- 238000005259 measurement Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 claims 1
- 230000000717 retained effect Effects 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 25
- 238000000034 method Methods 0.000 description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 19
- 238000005516 engineering process Methods 0.000 description 9
- 239000002351 wastewater Substances 0.000 description 9
- 239000005416 organic matter Substances 0.000 description 7
- 244000005700 microbiome Species 0.000 description 5
- 230000015556 catabolic process Effects 0.000 description 4
- 238000006731 degradation reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 238000011068 loading method Methods 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 238000005276 aerator Methods 0.000 description 3
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 229920002521 macromolecule Polymers 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000004060 metabolic process Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000005261 decarburization Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000005446 dissolved organic matter Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002846 particulate organic matter Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000010734 process oil Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/36—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
- C02F2103/365—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds from petrochemical industry (e.g. refineries)
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/08—Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1278—Provisions for mixing or aeration of the mixed liquor
-
- 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
- C02F3/28—Anaerobic digestion processes
- C02F3/2846—Anaerobic digestion processes using upflow anaerobic sludge blanket [UASB] reactors
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)
Abstract
The invention provides a kind of oil refining sewerage biological treatment device, hydrolysis acidification unit, aeration unit, primary deposition unit, LINPOR units and final precipitation unit, the hydrolysis acidification unit, the aeration unit, the primary deposition unit, the LINPOR units and the final precipitation unit are sequentially connected, Sludge Bed is provided with the hydrolysis acidification unit, sewage is retained and adsorbed after entering rising from the bottom of the hydrolysis acidification unit by the Sludge Bed, the particulate matter and colloidal substance that the Sludge Bed will be flowed into sewage；Pure oxygen is passed through in the aeration unit.
Description
Technical field
The present invention relates to a kind of oil refining sewerage biological treatment device, more particularly, to the life of Petrochemical Enterprises externally discharged waste water
Thing denitrogenation and decarburization.
Background technology
During produce reality, the characteristic for oil refining sewerage takes corresponding appropriate treatment technology, to go
Except the pollutant in processing sewage, so as to meet the purpose of qualified discharge or reusing sewage.Traditional Petrochemical Enterprises
Sewage Biological Treatment use biologic treating technique based on " activated sludge process ".With crude oil
Become weight and refine oil continuing to develop for deep process technology, the blowdown flow rate and pollutant concentration of each process units and pollution
Thing composition is all significantly increased, and with increasingly strict environmental requirement, " activated sludge process " is hard to carry on.Pass
System activated sludge process exist take up an area larger, surplus sludge volume it is many, to the biochemical oxygen demand (BOD) (BOD) in sewage
With COD (COD) treatment degradation effect it is undesirable, energy consumption is higher, investment is big, removal efficiency of nitrogen and phosphorus
Relatively low and poor to the change adaptation of waste water quality water problem.
The content of the invention
The technical problems to be solved by the invention are directed to the drawbacks described above of prior art, there is provided one kind oil refining
Biological sewage treatment device, the device can realize that Biodegradability of Wastewater is higher, COD clearances are high, dirt
Water can qualified discharge purpose.
To achieve these goals, the invention provides a kind of oil refining sewerage biological treatment device, including：Water
Solution acidifying unit, aeration unit, primary deposition unit, LINPOR units and final precipitation unit, it is described
Hydrolysis acidification unit, the aeration unit, the primary deposition unit, LINPOR units and described
Final precipitation unit is sequentially connected, and Sludge Bed is provided with the hydrolysis acidification unit, and sewage is sour from the hydrolysis
The bottom of change unit will flow into the particulate matter in sewage after entering rising by the Sludge Bed, the Sludge Bed
Matter and colloidal substance retention and absorption；Pure oxygen is passed through in the aeration unit.
Above-mentioned oil refining sewerage biological treatment device, the aeration unit is a pure oxygen aeration pond, using pure oxygen
The pure oxygen aeration pond is passed through instead of air, the pure oxygen aeration pond is three sections of closed ponds of series connection.
Above-mentioned oil refining sewerage biological treatment device, the LINPOR units are a LINPOR oxidation ponds,
The LINPOR oxidation ponds bottom of pond portion is provided with an aerator.
Above-mentioned oil refining sewerage biological treatment device, porous polyurethane is additionally provided with the LINPOR oxidation ponds
Filler.
Above-mentioned oil refining sewerage biological treatment device, the porous polyurethane filler is spongy block, long 1.
5cm, width 1.5cm, 1.2cm high.
Above-mentioned oil refining sewerage biological treatment device, the porous polyurethane filler is located in a filter.
Above-mentioned oil refining sewerage biological treatment device, the hydrolysis acidification unit is a hydrolysis acidification reaction tank,
The Waste water treatment amount of the hydrolysis acidification reaction tank is 300m3/ h, the pond body chi of the hydrolysis acidification pool
Very little is 31.5m × 10m × 5.5m, and effective liquid level of the hydrolysis acidification reaction tank is 5.1m, the hydrolysis
The dischargeable capacity in acidification reaction pond is 1530m3。
Above-mentioned oil refining sewerage biological treatment device, the size in each closed pond is 15.6m × 15.6
M × 6m, effective liquid level in the closed pond is 4.4 meters, three effective total measurement (volume)s 3 in the closed pond
210m3。
Above-mentioned oil refining sewerage biological treatment device, the Waste water treatment amount of the LINPOR oxidation ponds is
600m3/ h, the size of the LINPOR oxidation ponds is 19.2m × 15.6m × 7m, the LINPOR
Effective liquid level of oxidation pond is 6m, and the dischargeable capacity of the LINPOR oxidation ponds is 1800m3, it is passed through institute
The air demand for stating LINPOR oxidation ponds is 2500Nm3/ h, the porous poly- ammonia in the LINPOR oxidation ponds
Fat filler cumulative volume is 360m3。
Above-mentioned oil refining sewerage biological treatment device, the LINPOR oxidation ponds are provided with extruding demoulding pump, institute
State after porous polyurethane filler is extruded through the extruding demoulding pump to improve the renewal speed of biomembrane.
Beneficial functional of the invention is：
Apparatus of the present invention are used to process oil refining sewerage, can improve Biodegradability of Wastewater energy, after processing device
Substantially, water outlet can reach for the reduction of water outlet COD value, denitrification effect《Integrated wastewater discharge standard》GB897
8-96 secondary standards.
Brief description of the drawings
Fig. 1 is the oil refining sewerage biological treatment device schematic flow sheet of invention.
Specific embodiment
Structural principle of the invention and operation principle are described in detail below in conjunction with the accompanying drawings：
Can realize that Biodegradability of Wastewater is higher, COD clearances are high it is an object of the invention to provide one kind,
Sewage can qualified discharge oil refining sewerage biological treatment device.
The oil refining sewerage biological treatment device, the device includes the hydrolysis acidification unit, the aeration list that are sequentially connected
Unit, primary deposition unit, LINPOR units and final precipitation unit.
Hydrolysis acidification unit in the oil refining sewerage biological treatment device is a hydrolysis acidification reaction tank, hydrolysis
Acidizing Process Technique is to be subject to a kind of improved sewage disinfection treatment technology on the basis of anaerobic technology, of the invention
The treatment water of hydrolysis acidification pool is 300m3/ h, the size of hydrolysis acidification pool is 31.5m × 10m × 5.5m,
Effective liquid level of hydrolysis acidification pool is 5.1m, and the dischargeable capacity of hydrolysis acidification pool is 1530m3, sewage exists
The hydrolysis acidification pool residence time is 5.1h.Due to hydrolysis acidification reaction tank, to be belonging to upflow anaerobic sludge blanket process anti-
The technology category of device is answered, multiple injection well downhole flow regulators are provided with hydrolysis acidification reaction tank, a diameter of 1m of injection well downhole flow regulator matches somebody with somebody
Hydrophone quantity is 15, and water distribution uses pressure type water dispensing apparatus.Sewage by hydrolysis acidification reaction tank bottom
Into by Sludge Bed, the particulate matter and colloidal substance in water inlet are retained rapidly and inhaled by a large amount of microorganisms
Attached, this is a fast reaction for physical process, general only to need to complete within several seconds to tens seconds, is cut
The material for leaving is adsorbed on the surface of Sludge Bed, because these materials are attracted to Sludge Bed surface, so
Residence time in device is greater than hydraulic detention time, and be decomposed metabolism at leisure.Largely hydrolyzing micro- life
By insoluble hydrolysis of organic matter into solable matter in the presence of thing, while under the synergy of acid-producing bacteria
By macromolecular substances, it is difficult to degradable chemical and is converted into the small-molecule substance that is readily biodegradable, releases again
It is put into liquid, enters in postorder handling process with sewage.Because microorganism is while degradation of organic substances,
Increase breeding with organic matter as what substrate carried out itself, can make the sludge quantity of hydrolysis unit increases, thus will
This amount of activated sludge enters sludge condensation and dewatering unit.In this course, dissolubility BOD, CO
Although the clearance of D is anecdotally very low, hydrolysis acid is increased because particulate organic matter occurs hydrolysis
Change the concentration of dissolved organic matter in cell arrangement, therefore, dissolubility BOD, COD clearance is actually
It is very high.Hydrolysis acidification method of the invention be it is a kind of between method aerobic and between Anaerobic Treatment method, it is and straight
Anaerobic Treatment is connect to compare, it is short with hydraulic detention time, the advantages of floor space is small；With direct Aerobic Process for Treatment
Compare, have the advantages that Biodegradability of Wastewater energy, strong shock resistance can be improved.Hydrolysis acidification reaction tank collection
, in one, organic matter is in hydrolysis acidification reaction tank for precipitation, absorption, bioflocculation, biological degradation function
Removal includes physics, chemical and biochemical combined reaction process, i.e., using hydrolysis and acid-producing microorganisms,
By the solid in sewage, macromolecular and to be difficult biodegradable organic matter degradation be readily biodegradable small point
Sub- organic matter so that sewage is obtained with less energy consumption and under the shorter residence time in follow-up aerobic unit
Treatment.
Aeration unit in the oil refining sewerage biological treatment device, aeration unit is a pure oxygen aeration pond, and this is pure
Oxygen aeration tank is three sections of closed ponds of series connection, and pure oxygen aeration is the activity being aerated instead of air using pure oxygen
Sludge, because the partial pressure of oxygen in pure oxygen aeration is big, the rate of transform is high, makes that high concentration can be kept in aeration tank
Dissolved oxygen and high sludge concentration, therefore pure oxygen aeration pool volume is small, and floor space is small.And pure oxygen aeration
The oxygen for being used is air separation unit accessory substance, if do not utilized, is then processed by emptying, wastes the energy, and
Energy consumption and operating cost for can then reduce purified water herein.Meanwhile, from pure oxygen aeration petrochemical industry at home
From the point of view of the practical situations of enterprise, its treatment effeciency is high, impact resistance is good, it is stable the characteristics of
Confirmed.The treatment water in pure oxygen aeration pond is 600m3/ h, each closed pond pond body size is
15.6m × 15.6m × 6m, effective liquid level in each closed pond is 4.4m, three total effective appearances in closed pond
Product is 3210m3, sewage is 6h in the aeration unit residence time, and the activated sludge of unit mass is in unit
It is 0.3kgBOD/ [kgMLVSSd] for volumetric loading is that the amount of interior removed pollutant is sludge loading
1.8kgBOD/m3.d, concentration of suspension is 6000mg/L, and sludge is 5.3h in the aeration unit residence time,
Oxygen demand is 1.45kgO2/ kgBOD, sludge output is the dry mud/kgBOD of 0.4kg, return sludge ratio：100%.
LINPOR units in the oil refining sewerage biological treatment device, LINPOR units are a LINPOR
Oxidation pond, LINPOR oxidation ponds use a kind of technology similar with contact oxidation technology, and the technique is
Based on the principle of original sewage-treatment plant aerator active microorganism, by special porous polyurethane filler
Insert in aeration tank, porous polyurethane filler is stopped by the filter of particular design in pond.LINPOR oxidation ponds
Bottom is provided with aerator, and air is provided for it by air blower, activated sludge on porous polyurethane filler surface and
Growth inside, and grown in the form of suspension flco, the activated sludge of fixed growth and suspension growth is always dense
Degree is about the twice of traditional activated sludge process sludge concentration, and organic loading also increases about 34%, so that complete
Into biological denitrificaion and carbonization treatment.The LINPOR oxidation ponds are using the life being attached on porous polyurethane filler
Thing film processes pollutant.The porous polyurethane filler is spongy block, and size is
1.5cm × 1.5cm × 1.2cm, with very big specific surface area, make can be kept in LINPOR oxidation ponds compared with
Biomass high and abundant microbial population, are particularly conducive to breed the life of generation time microorganism long
It is long, such as remove the nitrifier of ammonia nitrogen and the flora of decomposition hardly degraded organic substance.LINPOR oxidation ponds also have
It is not easily blocked, the characteristics of without backwashing, and is provided with extruding demoulding pump, porous polyurethane filler is through squeezing
After the extruding of pressure-off membrane pump, the renewal of biomembrane is accelerated, and improves bioactivity.LINPOR oxidation technologies exist
Be there is no in Domestic Petrochemical Enterprises and apply achievement, but answered in municipal wastewater and external coked waste water at home
With operational effect is good, to ammonia nitrogen removal efficiency high.The treatment water of LINPOR oxidation ponds：600m3/ h,
The pond body size of LINPOR oxidation ponds is 19.2m × 15.6m × 7m, effective liquid level of LINPOR oxidation ponds
It is 6m, the dischargeable capacity of LINPOR oxidation ponds is 1800m3, dwell time of sewage is 3h (more than
Asked), porous polyurethane packing volume is 360m3, volumetric loading is 0.48kgNH4-N/m3.d, filler
Residence time is 3h, and air demand is 2500Nm3/h。
As shown in Figure 1, technological process is as described below for the oil refining sewerage biological treatment device that the present invention is provided：
Oil refining sewerage is entered by the bottom of pond of hydrolysis acidification pool and rises through Sludge Bed, and water distribution is matched somebody with somebody using pressure type
Water installations, particulate matter and colloidal substance in oil refining sewerage are trapped when by Sludge Bed, adsorbed, divided
Solution metabolism, insoluble hydrolysis of organic matter macromolecular substances, is difficult to biodegradable thing into solable matter
Matter is converted into the small-molecule substance being readily biodegradable.In this course, dissolubility BOD, COD
Clearance is very low, but the biodegradability of sewage is improved, and is that follow-up Aerobic Process for Treatment operation creates advantage.
Sewage after being processed through hydrolysis acidification pool flow to pure oxygen aeration pond, and the sewage after being processed through pure oxygen aeration pond flow to
Preliminary sedimentation tank carries out mud-water separation, and preliminary sedimentation tank water outlet gravity flow enters LINPOR oxidation ponds, in pure oxygen
Although the biochemical organic matter of the overwhelming majority has been removed in aeration tank, there is hardly degraded organic substance in sewage
With ammonia nitrogen need removal, particularly in view of saline sewage biodegradability it is poor the characteristics of, LINPOR oxidation
Pond is a kind of advanced reliable handling process.The water outlet of LINPOR oxidation ponds enters final precipitation unit, through prison
Survey qualified rear outer row.Its sewage disposal process of oil refining sewerage biological treatment device that the present invention is provided is " sewage
Water inlet → hydrolysis acidification pool → pure oxygen aeration pond → preliminary sedimentation tank → LINPOR oxidation ponds → final precipitation
Unit → outer row ", water outlet reaches《Integrated wastewater discharge standard》Outer row after GB8978-96 secondary standards.
Certainly, the present invention can also have other various embodiments, in the feelings without departing substantially from spirit of the invention and its essence
Under condition, those of ordinary skill in the art work as can make various corresponding changes and deformation according to the present invention, but
These corresponding changes and deformation should all belong to the protection domain of appended claims of the invention.
Claims (10)
1. a kind of oil refining sewerage biological treatment device, it is characterised in that including：Hydrolysis acidification unit, exposure
Gas unit, primary deposition unit, LINPOR units and final precipitation unit, the hydrolysis acidification unit,
The aeration unit, the primary deposition unit, the LINPOR units and the final precipitation unit according to
Secondary connection, is provided with Sludge Bed in the hydrolysis acidification unit, sewage enters from the bottom of the hydrolysis acidification unit
Enter by the Sludge Bed after rising, the particulate matter and colloidal substance that the Sludge Bed will be flowed into sewage cut
Stay and adsorb；Pure oxygen is passed through in the aeration unit.
2. oil refining sewerage biological treatment device as claimed in claim 1, it is characterised in that the aeration
Unit is a pure oxygen aeration pond, and the pure oxygen aeration pond, the pure oxygen aeration are passed through instead of air using pure oxygen
Pond is three sections of closed ponds of series connection.
3. oil refining sewerage biological treatment device as claimed in claim 1, it is characterised in that described
LINPOR units are a LINPOR oxidation ponds, and the bottom of pond portion of the LINPOR oxidation ponds is provided with an aeration
Device.
4. oil refining sewerage biological treatment device as claimed in claim 3, it is characterised in that described
Porous polyurethane filler is additionally provided with LINPOR oxidation ponds.
5. oil refining sewerage biological treatment device as claimed in claim 4, it is characterised in that described porous
Polyurethane filler is spongy block, 1.5cm long, width 1.5cm, 1.2cm high.
6. oil refining sewerage biological treatment device as claimed in claim 5, it is characterised in that described porous
Polyurethane filler is located in a filter.
7. oil refining sewerage biological treatment device as claimed in claim 1, it is characterised in that the hydrolysis
Acidifying unit is a hydrolysis acidification reaction tank, and the Waste water treatment amount of the hydrolysis acidification reaction tank is
300m3/ h, the pond body size of the hydrolysis acidification pool is 31.5m × 10m × 5.5m, the hydrolysis acidification reaction
Effective liquid level in pond is 5.1m, and the dischargeable capacity of the hydrolysis acidification reaction tank is 1530m3。
8. oil refining sewerage biological treatment device as claimed in claim 2, it is characterised in that each described
The size in closed pond is 15.6m × 15.6m × 6m, and effective liquid level in the closed pond is 4.4 meters, three
Effective total measurement (volume) 3210m in the individual closed pond3。
9. oil refining sewerage biological treatment device as claimed in claim 4, it is characterised in that described
The Waste water treatment amount of LINPOR oxidation ponds is 600m3/ h, the size of the LINPOR oxidation ponds is
19.2m × 15.6m × 7m, effective liquid level of the LINPOR oxidation ponds is 6m, the LINPOR oxygen
The dischargeable capacity for changing pond is 1800m3, the air demand for being passed through the LINPOR oxidation ponds is 2500Nm3/ h,
Porous polyurethane filler cumulative volume in the LINPOR oxidation ponds is 360m3。
10. oil refining sewerage biological treatment device as claimed in claim 4, it is characterised in that described
LINPOR oxidation ponds are provided with extruding demoulding pump, and the porous polyurethane filler is extruded through the extruding demoulding pump
Afterwards improving the renewal speed of biomembrane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510983379.7A CN106915863A (en) | 2015-12-24 | 2015-12-24 | A kind of oil refining sewerage biological treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510983379.7A CN106915863A (en) | 2015-12-24 | 2015-12-24 | A kind of oil refining sewerage biological treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106915863A true CN106915863A (en) | 2017-07-04 |
Family
ID=59456998
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510983379.7A Pending CN106915863A (en) | 2015-12-24 | 2015-12-24 | A kind of oil refining sewerage biological treatment device |
Country Status (1)
| Country | Link |
|---|---|
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| US20090272687A1 (en) * | 2006-10-30 | 2009-11-05 | Chiang Ming-Hui | Method of Deep Sewage Treatment without Sludge Discharge and Device Therefor |
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| CN205420083U (en) * | 2015-12-24 | 2016-08-03 | 中国石油天然气股份有限公司 | Oil refining sewage biological processing device |
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| US20090272687A1 (en) * | 2006-10-30 | 2009-11-05 | Chiang Ming-Hui | Method of Deep Sewage Treatment without Sludge Discharge and Device Therefor |
| CN103508618A (en) * | 2012-06-27 | 2014-01-15 | 中国石油化工股份有限公司 | Method for treating high-concentration ammonia nitrogen wastewater |
| CN103951061A (en) * | 2014-04-30 | 2014-07-30 | 中国石油天然气集团公司 | In-situ upgraded treatment method for realizing zero discharge of refinery and chemical wastewater and biological stuffing used in in-situ upgraded treatment method |
| CN205420083U (en) * | 2015-12-24 | 2016-08-03 | 中国石油天然气股份有限公司 | Oil refining sewage biological processing device |
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