CN111362438A - Electro-desalting wastewater oil removal treatment system and process - Google Patents
Electro-desalting wastewater oil removal treatment system and process Download PDFInfo
- Publication number
- CN111362438A CN111362438A CN202010190875.8A CN202010190875A CN111362438A CN 111362438 A CN111362438 A CN 111362438A CN 202010190875 A CN202010190875 A CN 202010190875A CN 111362438 A CN111362438 A CN 111362438A
- Authority
- CN
- China
- Prior art keywords
- oil
- desalting wastewater
- sedimentation tank
- membrane
- sludge
- 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
- 239000002351 wastewater Substances 0.000 title claims abstract description 101
- 238000011033 desalting Methods 0.000 title claims abstract description 91
- 238000000034 method Methods 0.000 title claims abstract description 76
- 230000008569 process Effects 0.000 title claims abstract description 40
- 238000000926 separation method Methods 0.000 claims abstract description 86
- 239000012528 membrane Substances 0.000 claims abstract description 79
- 238000001914 filtration Methods 0.000 claims abstract description 68
- 238000004062 sedimentation Methods 0.000 claims abstract description 65
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 63
- 239000010802 sludge Substances 0.000 claims abstract description 46
- 238000005374 membrane filtration Methods 0.000 claims description 15
- 238000011084 recovery Methods 0.000 claims description 13
- 230000005484 gravity Effects 0.000 claims description 9
- 238000007667 floating Methods 0.000 claims description 8
- 241000894006 Bacteria Species 0.000 claims description 7
- 238000005238 degreasing Methods 0.000 claims description 6
- 230000000694 effects Effects 0.000 abstract description 16
- 239000010865 sewage Substances 0.000 abstract description 12
- 239000003814 drug Substances 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 230000007547 defect Effects 0.000 abstract description 5
- 239000003921 oil Substances 0.000 description 148
- 239000000463 material Substances 0.000 description 19
- 239000002245 particle Substances 0.000 description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 238000001179 sorption measurement Methods 0.000 description 7
- 239000000839 emulsion Substances 0.000 description 6
- 239000010779 crude oil Substances 0.000 description 5
- 238000001556 precipitation Methods 0.000 description 5
- 150000003839 salts Chemical class 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 238000005345 coagulation Methods 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 239000006249 magnetic particle Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 238000006124 Pilkington process Methods 0.000 description 3
- 239000011358 absorbing material Substances 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 230000005684 electric field Effects 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000020477 pH reduction Effects 0.000 description 3
- -1 polypropylene Polymers 0.000 description 3
- 238000005185 salting out Methods 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 229940037003 alum Drugs 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 238000005354 coacervation Methods 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 239000011790 ferrous sulphate Substances 0.000 description 2
- 235000003891 ferrous sulphate Nutrition 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 230000036571 hydration Effects 0.000 description 2
- 238000006703 hydration reaction Methods 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 2
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 2
- 239000011368 organic material Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- HNNQYHFROJDYHQ-UHFFFAOYSA-N 3-(4-ethylcyclohexyl)propanoic acid 3-(3-ethylcyclopentyl)propanoic acid Chemical compound CCC1CCC(CCC(O)=O)C1.CCC1CCC(CCC(O)=O)CC1 HNNQYHFROJDYHQ-UHFFFAOYSA-N 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical class O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- 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
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/046—Recirculation with an external loop
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention provides an oil removal treatment system and a process for electric desalting wastewater, wherein the treatment system comprises an oil separation sedimentation tank and a membrane filtering device; the oil separation sedimentation tank is communicated with the membrane filtering device through a connecting pipe, a water supply pump is arranged on the connecting pipe, the water supply pump is used for sending the electric desalting wastewater after the sludge is precipitated in the oil separation sedimentation tank into the membrane filtering device, and the membrane filtering device is used for filtering the precipitated electric desalting wastewater; a settling tank is arranged at the bottom of the oil-separating sedimentation tank; the scheme provided by the invention provides the oil removal treatment process for the electric desalting sewage of the refinery aiming at the defects of unsatisfactory treatment effect, large floor area, high medicament consumption, high sludge production, poor oil removal effect and the like of the existing treatment process, and has the advantages of short treatment process, stable effect, low medicament consumption, containerization, high automation degree and the like.
Description
Technical Field
The invention belongs to the technical field of electro-desalting wastewater oil removal treatment, and particularly relates to an electro-desalting wastewater oil removal treatment system and process.
Background
The electric desalting device is one of indispensable devices in a refinery, and the operation effect of the electric desalting device can affect the long-term, safe and stable operation of an oil refining production device to a great extent. The crude oil desalting process includes adding certain amount of demulsifier and water to dissolve salt in water at certain temperature and separating oil from water under the action of electric field, so as to reach the aim of desalting and dewatering crude oil. Along with the deterioration of crude oil properties at home and abroad, the existing electric desalting device and process are increasingly difficult to control the indexes of the salt content after crude oil removal and the oil content in sewage.
The electro-desalting wastewater is seriously emulsified with oil, and the oil exists in the wastewater in a dispersed state and an emulsified state, so that great influence is brought to subsequent biochemical treatment. Along with the obvious problem of the electric desalting wastewater, the oil removal treatment problem of the electric desalting wastewater draws more attention. The oil removal treatment of the traditional electro-desalting wastewater generally adopts the following steps: the demulsification-separation method comprises the following steps:
demulsification method for electro-desalting wastewater
1. High voltage electric field method
The method utilizes the attraction or repulsion action of electric field force on emulsion particles to make the fine oil particles mutually collide in motion, thereby destroying the hydration film and the double electric layer structure of the fine oil particles, leading the fine oil particles to be coalesced into larger oil particles which float on the water surface and achieving the purpose of oil-water stratification. The high voltage power supply can adopt alternating current, direct current or pulse power supply.
2. Emulsion breaking method by using medicament
The demulsifying agent method is to add demulsifier into the waste water to destroy the hydrated film and electric double layer of oil droplets and to make the oil droplets gather and become larger and separate from water. The demulsification of the agent is divided into salting-out method, coagulation method, salting-out-coagulation mixing method and acidification method; the method specifically comprises the following steps:
(1) salting out method: the salting-out method is to add salt electrolyte into the wastewater to destroy the hydration membrane of oil droplets, and the commonly used electrolyte comprises calcium chloride, magnesium chloride, sodium chloride, calcium sulfate, magnesium sulfate and the like;
(2) and a coacervation method: the coagulation method is to add flocculant into waste water and to combine oil droplets into polymer by means of the bridging effect of the flocculant. The flocculating agent is commonly used such as alum, polyaluminium chloride, activated silicic acid, polyacrylamide, ferrous sulfate, ferric chloride, magnesium alumina and the like. Studies have shown that alum treatment of the solubilised oil is effective when pH = 8.0-9.0, whereas ferrous sulfate can be used when pH = 8-10;
(3) and an acidification method: the acidification method is to add sulfuric acid, hydrochloric acid, acetic acid or naphthenic acid into the wastewater to destroy the boundary film of the emulsion oil droplets, so that the fatty acid soap is changed into fatty acid and separated out. The method reduces the pH value of the waste rate water, so the pH value needs to be adjusted by an alkaline agent after oil-water separation to reach the discharge standard;
(4) salting-out- -coacervation mixing method: salting-out-coagulation mixing method is to add salt electrolyte into waste water to demulsify the emulsion and then add coagulant to separate oil particles.
3. Centrifugation method
The centrifugal machine has two types, namely horizontal type and vertical type, and under the action of centrifugal force, a water phase is discharged from the outer layer of the centrifugal machine, and an oil phase is discharged from the middle part of the centrifugal machine. The structure of the centrifuge is relatively complex, so the method is not generally adopted in China.
Second, separation treatment after demulsification and oil removal
After the emulsion is demulsified and deoiled, the emulsion generally needs further treatment, and the treatment method and treatment equipment are also various, and can be summarized as follows:
1. gravity separation method
The gravity separation method is a method for separating by using the density difference of oil and water, and can be used for removing more than 60 oil particles and most of solid particles in wastewater. The most common apparatus for gravity separation is the oil interceptor. It utilizes the characteristic that oil is lighter than water to separate oil from water surface and skimming. The oil separation tank is mainly used for removing floating oil or emulsified oil after demulsification, has a plurality of forms, and mainly comprises a horizontal flow type oil separation tank (API), a parallel plate type oil separation tank (PPI), a corrugated inclined plate oil separation tank (CPI), a pressure difference automatic oil skimming device and the like; the method is suitable for floating oil and dispersed oil, and has stable effect, low operation cost and large equipment floor area.
2. Air float method
The air flotation method is a method in which a large number of fine bubbles are adsorbed on particles (oil droplets) to be removed, and pollutants are taken out of the water surface by the buoyancy of the gas, thereby achieving the purpose of separation. The air microbubbles are composed of nonpolar molecules, can be combined with hydrophobic oil to bring oil droplets to rise together, the floating speed can be improved by about thousand times, so that the oil-water separation efficiency is high, and the air floatation method can be classified into air-blowing air floatation, pressurized air floatation, electrolytic air floatation and the like according to different bubble generation modes. The air-blowing air floatation is to inject air into water by using an air blower, an air compressor and the like, and can also bring air into water by using a water pump water suction pipe and a water ejector. The electrolytic air floatation is to electrolyze water by an electrolytic cell, and to take pollutants out of the water surface by utilizing the tiny hydrogen and oxygen bubbles formed by electrolysis, the pressurized air floatation is to dissolve air in water under the pressurized condition, then to return to the normal pressure, and to separate the pollutants by utilizing a large amount of released micro bubbles. Among the air float processes, the pressurized air float process is mainly used at present. The method has the advantages of low power consumption, simple equipment and good effect, and is widely applied to the mature treatment process of oil field wastewater, petrochemical wastewater, food oil production wastewater and the like.
3. Adsorption process
The adsorption method is to adsorb oil in water by using an oleophilic material. The most commonly used adsorbing material is activated carbon, which has good oil absorption performance and can adsorb dispersed oil, emulsified oil and dissolved oil in wastewater, but the adsorbing capacity is limited (the oil is generally 30-80 mg/g), the activated carbon is expensive, and the regeneration is difficult, so the activated carbon is generally only used for treating low-concentration oily wastewater or deeply treating the low-concentration oily wastewater. Many studies on oil absorbents have been reported. The adsorption resin is a novel organic adsorption material developed in recent years, has good adsorption performance, is easy to regenerate and reuse, and can possibly replace activated carbon. In addition, coal, oil-absorbing felt, ceramsite, quartz sand, wood chips, straw and the like also have oil-absorbing performance and can be used as an adsorbing material. After the absorbing material absorbs oil and is saturated, some absorbing materials can be regenerated and reused, and some absorbing materials can be directly used as fuel.
4. Coarse grain method
The coarse granulation method (also called agglomeration method) is to make the oily waste water pass through a device filled with coarse granulation material to make the fine oil droplets in the waste water coalesce into large particles, so as to achieve the purpose of oil-water separation. The method is suitable for pretreatment of dispersed oil and emulsified oil. The technical key point is that the coarse grained material can be divided into fibrous and granular materials from the shape of the material; from the material properties, many researchers believe that the oleophilic and hydrophobic properties of the material surface are dominant. Furthermore, the contact angle of the oleophilic material with oil is preferably less than 70. When the oily wastewater passes through the material, fine oil particles are adsorbed on the surface of the material, oil droplets are gradually agglomerated and expanded to form an oil film through continuous collision, and finally the oil droplets are separated from the surface of the material and float on the water surface under the thrust of gravity and water flow, and the coarse grained materials can be further divided into inorganic materials and organic materials: the shape of the material can be made into granular, fibrous, tubular or cemented shapes, and polypropylene, anthracite, ceramsite, quartz sand and the like can be used as coarse grained fillers. The coarse graining oil removing device has the advantages of small volume, high efficiency, simple structure, no need of adding medicine, investment saving and the like. The disadvantage is that the packing is easily clogged, thus reducing the oil removal efficiency.
5. Electromagnetic adsorption method
The magnetic particles are mixed with the oily wastewater, oil droplets are adsorbed by the magnetic particles, then the oily magnetic particles are separated by a magnetic separation device, the sewage can be purified, and the oily magnetic particles are further treated, namely an electromagnetic adsorption method, which is rarely applied.
The traditional separation method has poor separation effect on emulsified oil, low standard reaching rate of the device, large amount of sludge generated by adding a medicament, and further increased salt content in sewage, has the defects of long process flow, large investment, medicament addition, poor adaptability to water quality fluctuation and the like, and has no related solution; there is therefore a pressing need to find effective solutions to the above problems.
Disclosure of Invention
The invention aims to provide an electro-desalting wastewater oil removal treatment system and process aiming at overcoming the defects in the prior art, and aims to overcome the defects of poor treatment effect, large occupied area, high medicament consumption, high sludge production, poor oil removal effect and the like in the conventional electro-desalting wastewater treatment process.
The invention provides an oil removal treatment system for electric desalting wastewater, which comprises an oil separation sedimentation tank and a membrane filtering device, wherein the oil separation sedimentation tank is connected with the membrane filtering device; the oil separation sedimentation tank is communicated with the membrane filtering device through a connecting pipe, a water supply pump is arranged on the connecting pipe, the water supply pump is used for sending the electric desalting wastewater after the sludge is precipitated in the oil separation sedimentation tank into the membrane filtering device, and the membrane filtering device is used for filtering the precipitated electric desalting wastewater; the bottom of the oil-separating sedimentation tank is provided with a sedimentation tank.
Furthermore, the treatment system also comprises a sludge treatment device, and the sedimentation tank has a conical structure; the sedimentation tank is communicated with the sludge treatment device and is used for sending the precipitated sludge into the sludge treatment device, and the sludge treatment device is used for dehydrating the sludge.
Further, the processing system also comprises an oil recovery device, and the oil recovery device is communicated with the upper end in the oil separation sedimentation tank through an oil recovery pipe.
Furthermore, a separation membrane is arranged in the membrane filtration device, and the filtration precision of the separation membrane is less than 50 nm.
Furthermore, the treatment system also comprises a water inlet pipe and a circulating pipe, wherein the water inlet pipe is communicated with the inside of the oil separation sedimentation tank through the upper end of the side wall of the oil separation sedimentation tank, one end of the circulating pipe is communicated with the water inlet pipe, and the other end of the circulating pipe is communicated with a concentration discharge port in the membrane filtering device.
Further, the membrane filtration device is also communicated with a biochemical system or a post-treatment device; the oil content of the electric desalting wastewater filtered by the membrane filtering device is less than 10 ppm.
Correspondingly, the invention also provides an electro-desalting wastewater oil removal treatment process which can be applied to the electro-desalting wastewater oil removal treatment system; the method also comprises the following steps:
s1: firstly, introducing the electro-desalting wastewater into an oil separation sedimentation tank through a water inlet pipe for sedimentation, so that oil gathered in the electro-desalting wastewater floats upwards, and sludge in the electro-desalting wastewater is sedimentated by gravity;
s2: starting a water supply pump, and sending the electro-desalting wastewater after the sludge is precipitated in the oil separation sedimentation tank into a membrane filtering device through a connecting pipe for filtering;
s3: the electric desalting wastewater filtered by the membrane filtering device enters a biochemical system or a post-treatment device, and concentrated water in the membrane filtering device returns to the oil separation sedimentation tank through a circulating pipe to be re-precipitated.
Further, the treatment process also comprises the following steps:
s4: the sludge treatment device is communicated with a sedimentation tank at the bottom of the oil-separating sedimentation tank, so that sludge in the sedimentation tank is collected;
s5: the oil recovery device is communicated with the upper end in the oil separation sedimentation tank through an oil recovery pipe, so that the floating oil is collected.
Furthermore, a separation membrane is arranged in the membrane filtering device and is used for filtering oil, suspended matters, bacteria and organic matters in the electric desalting wastewater.
Further, in the step S2, the oil content of the electric desalting wastewater filtered by the membrane filtering device is less than 10ppm, and then the electric desalting wastewater enters a biochemical system or a post-treatment device.
By adopting the technical scheme, the invention has the following beneficial effects:
the oil removal treatment system for the electro-desalting wastewater provided by the invention has the advantages of short whole treatment process, small occupied area and low system cost.
The electro-desalting wastewater oil removal treatment system and process provided by the invention have the advantages that impurities such as oil removal, suspended matters and the like are effectively filtered through a separation membrane through physical filtration.
Thirdly, the oil removal treatment system and the process for the electro-desalting wastewater provided by the invention can remove impurities such as oil, suspended matters and the like in the electro-desalting wastewater of a refinery at one time, and do not need to add chemicals during operation and increase the sludge amount; the membrane filtration process adopts circulating filtration to reduce the pollution of the membrane.
According to the system and the process for removing the oil from the electro-desalting wastewater, provided by the invention, the membrane concentrated solution returns to the oil separation tank for precipitation, so that sewage is not discharged during operation, and the pollution is reduced.
Drawings
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
The invention will be further explained with reference to the drawings, in which:
FIG. 1 is a schematic diagram of an oil removal treatment system for electric desalted wastewater according to the present invention;
FIG. 2 is a flow chart of the oil removing treatment process of the electro-desalting wastewater of the invention.
In the figure: 1. an oil-separating sedimentation tank; 11. a settling tank; 2. a water supply pump; 3. a membrane filtration device; 4. a connecting pipe; 5. a circulation pipe.
Detailed Description
It should be noted that the embodiments and features of the embodiments in the present application may be combined with each other without conflict. The present invention will be described in detail below with reference to the embodiments with reference to the attached drawings.
As shown in fig. 1 to 2, the present invention provides an oil removing treatment system for electric desalting wastewater, which is a treatment system for solving the problems of unsatisfactory treatment effect, large floor area, large medicament consumption, large sludge production, poor oil removing effect, etc. of the existing electric desalting wastewater treatment process of a refinery; the treatment system has small volume, is easy to skid-mount, and is suitable for the oil removal treatment of crude oil electric desalting sewage of refining enterprises; the system specifically comprises an oil separation sedimentation tank 1 and a membrane filtering device 3; the oil separation sedimentation tank 1 is communicated with the membrane filtering device 3 through a connecting pipe 4, a water supply pump 2 is arranged on the connecting pipe 4, the water supply pump 2 is used for sending the electric desalting wastewater after the sludge is precipitated in the oil separation sedimentation tank 1 into the membrane filtering device 3 for physical filtration, namely the membrane filtering device 3 is used for filtering the electric desalting wastewater after the precipitation, so that oil, suspended matters, colloids, macromolecular organic matters and the like in the electric desalting wastewater are removed; furthermore, a plurality of sedimentation tanks 11 are arranged at the bottom of the oil-separating sedimentation tank 1, and the sedimentation tanks 11 are used for collecting the precipitated sludge, so that the further treatment is facilitated; in the scheme, the refinery electro-desalting wastewater subjected to oil skimming and precipitation is sent to a membrane filtering device 3 by a water supply pump 2 for separation, a special separation membrane is filled in the membrane filtering device 3, the separation membrane has the characteristics of clear water, oil resistance, high temperature resistance, acid and alkali resistance and the like, the filtering precision is less than 50nm, and oil, suspended matters, bacteria and macromolecular organic matters in the refinery electro-desalting wastewater are removed after being filtered by the membrane filtering device; the scheme provided by the invention provides the oil removal treatment process for the electric desalting sewage of the refinery aiming at the defects of unsatisfactory treatment effect, large floor area, high medicament consumption, high sludge production, poor oil removal effect and the like of the existing treatment process, and has the advantages of short treatment process, stable effect, low medicament consumption, containerization, high automation degree and the like.
Preferably, in combination with the above scheme, as shown in fig. 1 to 2, the treatment system further comprises a sludge treatment device, the sedimentation tank 11 has a conical structure, and the conical structure has an effect of conveniently collecting sludge; further, the settling tank 11 is communicated with a sludge treatment device for sending the settled sludge into the sludge treatment device, and the sludge treatment device is used for dewatering the sludge so as to recover the sludge.
Preferably, in combination with the above scheme, as shown in fig. 1 to 2, the treatment system further comprises an oil recovery device which is communicated with the upper end in the oil separation sedimentation tank 1 through an oil recovery pipe so as to recover the oil floating in the oil separation sedimentation tank 1.
Preferably, in combination with the above scheme, in this embodiment, a separation membrane is disposed in the membrane filtration device 3, and the filtration precision of the separation membrane is less than 50nm, so that the separation membrane can effectively filter oil, suspended matters, bacteria and macromolecular organic matters in the electric desalting wastewater; specifically, the separation membrane is made of an organic material, and compared with the traditional organic membrane material, the hydrophilic performance of the separation membrane is greatly improved; further, the contact angle of the separation membrane was 31.6 °, and the contact angle of PVDF, which is a conventional membrane material, was 59.5 ° (the smaller the contact angle, the more hydrophilic); furthermore, the separation membrane material is uncharged, is more resistant to oil and organic matter swelling compared with the existing membrane material, can operate at the temperature of 90 ℃, is resistant to acid and alkali environments, and has the pH tolerance range of 1-13.5; further, the width of the membrane flow channel in the membrane filtration device 3 is at most 3mm, and the membrane flow channel is corrugated, so that more pollutants can pass through the membrane filtration device without blockage.
Preferably, in combination with the above scheme, as shown in fig. 1 to 2, the treatment system further comprises a water inlet pipe and a circulating pipe 5, the water inlet pipe is communicated with the oil separation sedimentation tank 1 through the upper end of the side wall of the oil separation sedimentation tank 1, one end of the circulating pipe 5 is communicated with the water inlet pipe, and the other end of the circulating pipe 5 is communicated with a concentration discharge port in the membrane filtering device 3, so that the concentrated water in the membrane filtering device 3 can be circulated to the oil separation sedimentation tank 1 for secondary sedimentation and filtration treatment.
Preferably, in combination with the above scheme, as shown in fig. 1 to 2, the membrane filtration device 3 is also communicated with a biochemical system or a post-treatment device, so as to further treat the wastewater after filtration and separation; the oil content of the electric desalting wastewater filtered by the membrane filtering device 3 is less than 10ppm, so that the filtering and separating standard is met; the wastewater precipitated and pumped by the oil separation sedimentation tank 1 is sent to a membrane filtering device 3 by a water supply pump 2 for separation, a special separation membrane is filled in the membrane filtering device 3, and the wastewater is clean water, oil resistance, high temperature resistance, acid and alkali resistance, the filtering precision is less than 50nm, and oil, suspended matters, bacteria and macromolecular organic matters in the return fluid are removed after the electric desalting wastewater of the refinery is filtered by the membrane device.
Correspondingly, in combination with the above solution, as shown in fig. 1 to fig. 2, an electro-desalting wastewater degreasing treatment process can be applied to the electro-desalting wastewater degreasing treatment system; the oil removal treatment process for the electro-desalting sewage of the refinery realizes effective separation and removal of oil and suspended matters in the electro-desalting sewage in the shortest flow, and is suitable for water quality fluctuation, no dosage during operation and no sludge increase; specifically, the treatment process comprises the following steps:
s1: firstly, introducing the electro-desalting wastewater into an oil separation sedimentation tank 1 through a water inlet pipe for sedimentation, floating the gathered oil by utilizing the specific gravity difference, and settling suspended matters by gravity; namely, the oil gathered in the electric desalting wastewater floats upwards, and the sludge of the electric desalting wastewater is precipitated by gravity;
s2: starting the water supply pump 2, and sending the electro-desalting wastewater after the sludge is precipitated in the oil separation sedimentation tank 1 into the membrane filtering device 3 through the connecting pipe 4 for filtering; specifically, the refinery electro-desalted sewage after oil skimming and precipitation is sent into a membrane filtering device 3 by a water supply pump 2 for separation, a special separation membrane is filled in the membrane filtering device, the separation membrane has the characteristics of clear water, oil resistance, high temperature resistance and acid and alkali resistance, the filtering precision of the separation membrane is less than 50nm, and oil, suspended matters, bacteria and macromolecular organic matters in the wastewater are removed after the refinery electro-desalted sewage is filtered by the membrane device;
s3: the electric desalting wastewater filtered by the membrane filtering device 3 enters a biochemical system or a post-treatment device for further treatment; specifically, the concentrated water in the membrane filtration device 3 is returned to the oil separation sedimentation tank 1 through the circulation pipe 5 for re-sedimentation, so that the concentrated water in the membrane filtration device 3 can be circulated to the oil separation sedimentation tank 1 for secondary sedimentation and filtration treatment.
Preferably, in combination with the above scheme, as shown in fig. 1 to 2, the treatment process further includes the following processes:
s4: the sludge treatment device is communicated with the sedimentation tank 11 at the bottom of the oil separation sedimentation tank 1 so as to collect the sludge in the sedimentation tank 11, and the sedimentation tank 11 is of a conical structure which has the function of conveniently collecting the sludge;
s5: the oil recovery device is communicated with the upper end in the oil separation sedimentation tank 1 through an oil recovery pipe, so that the floating oil is collected for further treatment.
Preferably, in combination with the above scheme, as shown in fig. 1 to 2, a separation membrane is arranged in the membrane filtration device 3, and the separation membrane is used for filtering oil, suspended matters, bacteria and organic matters in the electric desalting wastewater.
Preferably, in combination with the above scheme, as shown in fig. 1 to 2, in the step S2, the oil content of the electric desalting wastewater filtered by the membrane filtration device 3 is less than 10ppm, and then the electric desalting wastewater enters a biochemical system or a post-treatment device.
By adopting the technical scheme, the invention has the following beneficial effects:
the oil removal treatment system for the electro-desalting wastewater provided by the invention has the advantages of short whole treatment process, small occupied area and low system cost.
The electro-desalting wastewater oil removal treatment system and process provided by the invention have the advantages that impurities such as oil removal, suspended matters and the like are effectively filtered through a separation membrane through physical filtration.
Thirdly, the oil removal treatment system and the process for the electro-desalting wastewater provided by the invention can remove impurities such as oil, suspended matters and the like in the electro-desalting wastewater of a refinery at one time, and do not need to add chemicals during operation and increase the sludge amount; the membrane filtration process adopts circulating filtration to reduce the pollution of the membrane.
According to the system and the process for removing the oil from the electro-desalting wastewater, provided by the invention, the membrane concentrated solution returns to the oil separation tank for precipitation, so that sewage is not discharged during operation, and the pollution is reduced.
The above description is only a preferred embodiment of the present invention, and is not intended to limit the present invention in any way. Those skilled in the art can make numerous possible variations and modifications to the described embodiments, or modify equivalent embodiments, without departing from the scope of the invention. Therefore, any modification, equivalent change and modification made to the above embodiments according to the technology of the present invention are within the protection scope of the present invention, unless the content of the technical solution of the present invention is departed from.
Claims (10)
1. An electro-desalting wastewater oil removal treatment system is characterized by comprising an oil separation sedimentation tank (1) and a membrane filtering device (3); the oil separation sedimentation tank (1) is communicated with the membrane filtering device (3) through a connecting pipe (4), a water supply pump (2) is arranged on the connecting pipe (4), the water supply pump (2) is used for sending the electric desalting wastewater after the sludge is precipitated in the oil separation sedimentation tank (1) into the membrane filtering device (3), and the membrane filtering device (3) is used for filtering the precipitated electric desalting wastewater; and a settling tank (11) is arranged at the bottom of the oil separation settling tank (1).
2. The electro-desalting wastewater degreasing treatment system as set forth in claim 1, wherein the treatment system further comprises a sludge treatment device, the settling tank (11) is of a cone-shaped structure; the settling tank (11) is communicated with the sludge treatment device and is used for conveying settled sludge into the sludge treatment device, and the sludge treatment device is used for dewatering the sludge.
3. The electro-desalting wastewater degreasing treatment system as set forth in claim 1 or 2, wherein the treatment system further comprises an oil recovery device communicating with the upper end inside the oil-separating sedimentation tank (1) through an oil recovery pipe.
4. The electro-desalting wastewater degreasing treatment system as set forth in claim 1, wherein a separation membrane is disposed in the membrane filtration device (3), and the filtration precision of the separation membrane is less than 50 nm.
5. The oil removal treatment system for electric desalting wastewater according to claim 3, further comprising a water inlet pipe and a circulating pipe (5), wherein the water inlet pipe is communicated with the inside of the oil separation sedimentation tank (1) through the upper end of the side wall of the oil separation sedimentation tank (1), one end of the circulating pipe (5) is communicated with the water inlet pipe, and the other end of the circulating pipe (5) is communicated with a concentration discharge port in the membrane filtering device (3).
6. The electro-desalting wastewater degreasing treatment system as set forth in claim 1, wherein the membrane filtration device (3) is further communicated with a biochemical system or a post-treatment device; the oil content of the electric desalting wastewater filtered by the membrane filtering device (3) is less than 10 ppm.
7. An oil removing treatment process for electric desalting wastewater, which can be applied to the oil removing treatment system for electric desalting wastewater of any one of claims 1 to 6; the method is characterized by further comprising the following steps:
s1: firstly, introducing the electric desalting wastewater into an oil separation sedimentation tank (1) through a water inlet pipe for sedimentation, so that oil gathered in the electric desalting wastewater floats upwards, and sludge in the electric desalting wastewater is precipitated by gravity;
s2: starting the water supply pump (2), and sending the electro-desalting wastewater after the sludge is precipitated in the oil separation sedimentation tank (1) into the membrane filtering device (3) for filtering through the connecting pipe (4);
s3: the electric desalting wastewater filtered by the membrane filtering device (3) enters a biochemical system or a post-treatment device, and concentrated water in the membrane filtering device (3) returns to the oil separation sedimentation tank (1) through a circulating pipe (5) for re-sedimentation.
8. The oil removing treatment process for the electro-desalting wastewater as claimed in claim 7, further comprising the following steps:
s4: the sludge treatment device is communicated with a sedimentation tank (11) at the bottom of the oil separation sedimentation tank (1) so as to collect sludge in the sedimentation tank (11);
s5: the oil recovery device is communicated with the upper end in the oil separation sedimentation tank (1) through an oil recovery pipe, so that the floating oil is collected.
9. The oil removing treatment process for the electric desalting wastewater according to claim 7, wherein a separation membrane is arranged in the membrane filtering device (3), and the separation membrane is used for filtering oil, suspended matters, bacteria and organic matters in the electric desalting wastewater.
10. The oil removing treatment process of the electric desalting wastewater according to claim 7, wherein in the step S2, the oil content of the electric desalting wastewater filtered by the membrane filtering device (3) is less than 10ppm, and then the electric desalting wastewater enters a biochemical system or a post-treatment device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010190875.8A CN111362438A (en) | 2020-03-18 | 2020-03-18 | Electro-desalting wastewater oil removal treatment system and process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010190875.8A CN111362438A (en) | 2020-03-18 | 2020-03-18 | Electro-desalting wastewater oil removal treatment system and process |
Publications (1)
Publication Number | Publication Date |
---|---|
CN111362438A true CN111362438A (en) | 2020-07-03 |
Family
ID=71202687
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010190875.8A Pending CN111362438A (en) | 2020-03-18 | 2020-03-18 | Electro-desalting wastewater oil removal treatment system and process |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111362438A (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000263059A (en) * | 1999-03-17 | 2000-09-26 | Kurita Water Ind Ltd | Electric desalting apparatus |
RU2264993C1 (en) * | 2004-04-27 | 2005-11-27 | Государственное образовательное учреждение высшего профессионального образования Уфимский государственный нефтяной технический университет (ГОУ ВПО УГНТУ) | Method of purification of oily waste waters |
CN103102035A (en) * | 2011-11-10 | 2013-05-15 | 中国石油化工股份有限公司 | High acid crude oil electric desalting wastewater treatment method |
CN103755052A (en) * | 2014-01-26 | 2014-04-30 | 西安瑞蓝机电设备有限公司 | Method and system for treating petroleum refining wastewater electro-desalting black liquor |
CN109574321A (en) * | 2019-01-14 | 2019-04-05 | 华东理工大学 | Oil-mud-water three-phase integratedization separator and separation method |
CN110577309A (en) * | 2019-09-17 | 2019-12-17 | 北京大井易通科技发展有限公司 | Fracturing flow-back fluid treatment system and process |
CN212293036U (en) * | 2020-03-18 | 2021-01-05 | 北京大井易通科技发展有限公司 | Electro-desalting wastewater oil removal treatment system |
-
2020
- 2020-03-18 CN CN202010190875.8A patent/CN111362438A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000263059A (en) * | 1999-03-17 | 2000-09-26 | Kurita Water Ind Ltd | Electric desalting apparatus |
RU2264993C1 (en) * | 2004-04-27 | 2005-11-27 | Государственное образовательное учреждение высшего профессионального образования Уфимский государственный нефтяной технический университет (ГОУ ВПО УГНТУ) | Method of purification of oily waste waters |
CN103102035A (en) * | 2011-11-10 | 2013-05-15 | 中国石油化工股份有限公司 | High acid crude oil electric desalting wastewater treatment method |
CN103755052A (en) * | 2014-01-26 | 2014-04-30 | 西安瑞蓝机电设备有限公司 | Method and system for treating petroleum refining wastewater electro-desalting black liquor |
CN109574321A (en) * | 2019-01-14 | 2019-04-05 | 华东理工大学 | Oil-mud-water three-phase integratedization separator and separation method |
CN110577309A (en) * | 2019-09-17 | 2019-12-17 | 北京大井易通科技发展有限公司 | Fracturing flow-back fluid treatment system and process |
CN212293036U (en) * | 2020-03-18 | 2021-01-05 | 北京大井易通科技发展有限公司 | Electro-desalting wastewater oil removal treatment system |
Non-Patent Citations (1)
Title |
---|
马艳宁: "《酸洗废水处理工艺技术手册》", 中国环境出版社, pages: 45 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107129111B (en) | Physical method oil field water treatment standard-reaching device and treatment process | |
US20170088441A1 (en) | Method and device for deep oil removal from wastewater containing low concentration dirty oil | |
US8632685B2 (en) | Multistage DAF-advanced oxidation system | |
CN102730795B (en) | High precision oil and water separation device and method thereof | |
KR20160029272A (en) | a simple structured wastewater treatment system using multi step aerating floation method and the wastewater treatment method | |
CN112390420A (en) | System and method suitable for treating complex produced liquid of offshore gas field | |
KR20160032067A (en) | a simple structured wastewater treatment system using multi step aerating floation method and the wastewater treatment method | |
CN110078273A (en) | A kind of oil field ternary drives and infuses poly- sewage physical processing apparatus and processing method | |
CN110835209A (en) | Centralized treatment method and system for oily sewage of ship | |
CN204281479U (en) | A kind for the treatment of system of coating wastewater | |
CN212293036U (en) | Electro-desalting wastewater oil removal treatment system | |
CN105923830B (en) | A kind of preprocess method of coal chemical industrial waste water two-stage enhanced coagulation oil removing | |
CN103754986B (en) | A kind of Oil stain mixture separation system | |
KR20090011279A (en) | Apparatus for separating oil from water | |
CN217077213U (en) | Oily wastewater recycling and treating integrated device | |
CN111362438A (en) | Electro-desalting wastewater oil removal treatment system and process | |
CN114212853B (en) | Air floatation tank for demulsification of emulsified oil-containing wastewater, wastewater treatment system comprising air floatation tank and method | |
CN212712986U (en) | Oil removing and filtering system | |
CN210481098U (en) | Oil field ASP flooding and polymer injection sewage physical treatment device | |
CN112624406A (en) | Deep purification method and device for drilling sewage | |
CN201704138U (en) | Airtight sewage treatment device for tank car mechanical cleaning | |
Wu et al. | Treatment of Refined oil depot wastewater | |
CN214936479U (en) | Novel atmospheric and vacuum electro-desalting sewage deep oil-water separation equipment | |
CN217479193U (en) | Oil removing device for treatment of produced water of offshore drilling platform | |
CN1312226A (en) | Counter-current air floating water-treating method and apparatus |
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 | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20200703 |