CN105384299A - Oil-containing sewage integrated purifier - Google Patents
Oil-containing sewage integrated purifier Download PDFInfo
- Publication number
- CN105384299A CN105384299A CN201510938908.1A CN201510938908A CN105384299A CN 105384299 A CN105384299 A CN 105384299A CN 201510938908 A CN201510938908 A CN 201510938908A CN 105384299 A CN105384299 A CN 105384299A
- Authority
- CN
- China
- Prior art keywords
- water
- sewage
- oil
- mud
- reaction cabin
- 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
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
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- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
-
- 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
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/32—Hydrocarbons, e.g. oil
-
- 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
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
-
- 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
Abstract
The invention discloses an oil-containing sewage integrated purifier. The oil-containing sewage integrated purifier has a purification tower structure. The upper part of the purifier is provided with a water collection tank (6) and an oil collection tank (7). The position of the oil collection tank (7) is higher than that of the water collection tank (6). The middle of the purifier is a reaction cabin (5). An outlet of the upper part of the reaction cabin (5) is respectively connected to the water collection tank (6) and the oil collection tank (7). One side of the purifier is provided with a sewage inlet pipe (1). The sewage inlet pipe (1) stretches into the purifier and is connected to the reaction cabin (5). The bottom of the reaction cabin is provided with a dredge pipe (3). Sediment separated from the muddy water is discharged by the dredge pipe (3). One side of the purifier is provided with an overflow pipe (4) and a water outlet pipe (2). When the water level in the tank is higher than the oil collection tank, water is discharged.
Description
Technical field
The present invention relates to environmental protection and resources domain, especially relate to a kind of oily(waste)water integral purifier.
Background technology
Along with society and industrial expansion, the increase of world population and improving constantly of people's living standard brought thus, the mankind constantly increase for the consumption of all kinds of water resources, and the Freshwater resources that the mankind depend on for existence are just being tending towards exhausted.China is the country that world population is maximum; the amount of per capita Freshwater resources is extremely limited; well below world average level; the Freshwater resources of China are faced with severe tests; although government strengthens the management for Freshwater resources by various method and measure; society has also recognized the seriousness that water resources lacks, and wants the Freshwater resources protecting our only preciousness.In addition, energy strategy is also national basic strategy means, and the recycling how carrying out the energy is also a vital problem.
In actual life, often there will be the situation of water and oil phase mixing, such as, when marine oil is revealed, waterbornely have large-area oil mixing with water, not only can cause a large amount of energy dissipations, and to neighbouring water body, there is great pollution.In addition, be all outwell simply after the oil in a lot of restaurant is mixed with water, its waste caused is very big, and very big in blowdown aftertreatment ground difficulty.
Summary of the invention
In order to overcome the deficiencies in the prior art, the invention provides a kind of oily(waste)water integral purifier, this equipment is the professional equipment of the water resources process of administering oil field and various industrial pollution.
The technical solution adopted for the present invention to solve the technical problems is: a kind of oily(waste)water integral purifier, this cleaner is tank structure, the top of described cleaner is provided with water leg and oil trap, the position of oil trap is higher than water leg, the middle part of described cleaner is reaction cabin, export above reaction cabin and connect water leg and oil trap respectively, the side of cleaner is provided with sewage water inlet pipe and shore pipe, sewage water inlet pipe stretches into cleaner and is connected with reaction cabin, shore pipe is provided with bottom reaction cabin, the outlet of shore pipe is outside tank body, silt after mud-water separation is discharged by shore pipe, the side of cleaner is provided with upflow tube and rising pipe, in tank body, water level begins through upflow tube water outlet after exceeding oil trap, described water leg connects rising pipe, water leg, two pipelines that oil trap connects are directly through reaction cabin, in the bottom water outlet of tank body.
Above described reaction cabin, outlet can be arranged the sewage in rotation and be formed microelectronics cloud filtering layer, when mud enters into microelectronics cloud filtering layer time, mud is in continuous exclusion process, electrostatic field can be formed, and electronic cloud distortion above mud layer, can be formed, carry out adsorpting polymerization to the particulate matter in sewage, electric charge actual interacted sewage purification and filtration, the sewage after filtration rises to water outlet and completes water outlet.
The process that oily(waste)water integral purifier is purified waste water is, sewage lagoon sewage is by adding sterilant, remove bacterium in water, stabilizing water quality, then flocculation agent is added, the oil in sewage, suspended particle, oil in water emulsion mixture adsorbs, impurity absorption in sewage is formed the floc sedimentation of bulk, then add coagulant aids flco is increased the weight of, make sewage after entering oily(waste)water integral purifier, advance in the direction predetermined according to water trap, enter reaction cabin, mud discharging device is provided with bottom reaction cabin, by a small amount of spoil disposal, form downward gravity, mud is due to own wt, carry out mud-water separation, mud is made up of the impurity in medicament and sewage, mud layer is upwards in process, above reaction cabin, outlet can be arranged the sewage in rotation and be formed microelectronics cloud filtering layer, when mud enters into microelectronics cloud filtering layer time, mud is in continuous exclusion process, electrostatic field can be formed, and electronic cloud distortion above mud layer, can be formed, adsorpting polymerization is carried out to the particulate matter in sewage, electronic cloud filters the gravitation deriving from moment of dipole generation and comprises electric charge, dipole and its interaction of quadrupole moment are pressed 1/kT power exponent by Boltzmann weighting factor and are launched, electric charge actual interacted sewage purification and filtration, sewage after filtration rises to water outlet, complete water outlet.
Impurity in sewage and medicament produce adsorptive power, adsorptive power produces electric charge, charges generate magnetic fields, the microelectronics magnetic field in magnetic field, namely electronic cloud filtering layer, impurity in sewage can all adsorb by described microelectronics filtering layer, the oil of 99% also can adsorb, remaining a small amount of oil bloom upwards always, the gravity principle that water leg utilizes, oil bloom float, water outlet pipeline can not be entered, oil bloom rise always, rise to oil trap, regular discharge, approximately monthly oil extraction once, microelectronics cloud filtering layer is due to medicament, mud, sump oil forms, in operational process, reaction cabin discharges a part, equipment is stopped transport and is discharged major part, device start, automatic formation, the distance of reaction cabin distance set tank, it is exactly the amount of water outlet, the microelectronics filtering layer formation time of reaction cabin is after device start about 15 minutes, and the distance of water leg and reaction cabin is large, there is the water discharging time of 2 hours.
Beneficial effect of the present invention: the present invention solves the process problem of industrial sewage and oil field extracted water, and cost of disposing of sewage is low, can reach the oil field extracted water cleanup standard of national regulation.This equipment runs simple, and be easy to operational management, failure rate is low, do not need filtrate, life of equipment is long.Safe and reliable, energy-conserving and environment-protective are standard equipments of sewage disposal aspect of new generation.
Accompanying drawing explanation
In order to be illustrated more clearly in the embodiment of the present invention or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is oily(waste)water integral purifier structural map of the present invention.
Embodiment
Below in conjunction with embodiment, the present invention is further described.
Embodiment 1
As shown in Figure 1, a kind of oily(waste)water integral purifier, this cleaner is tank structure, the top of described cleaner is provided with water leg 6 and oil trap 7, the position of oil trap 7 is higher than water leg 6, the middle part of described cleaner is reaction cabin 5, export above reaction cabin and connect water leg 6 and oil trap 7 respectively, sewage water inlet pipe 1 and shore pipe 3 is provided with in the side of cleaner, sewage water inlet pipe stretches into cleaner and is connected with reaction cabin 5, shore pipe 3 is provided with bottom reaction cabin, the outlet of shore pipe 3 is outside tank body, silt after mud-water separation is discharged by shore pipe 3, upflow tube 4 and rising pipe 2 is provided with in the side of cleaner, in tank body, water level begins through upflow tube 4 water outlet after exceeding oil trap, described water leg 6 connects rising pipe 2, water leg 6, two pipelines that oil trap 7 connects are directly through reaction cabin 5, in the bottom water outlet of tank body.
Above described reaction cabin, outlet can be arranged the sewage in rotation and be formed microelectronics cloud filtering layer, when mud enters into microelectronics cloud filtering layer time, mud is in continuous exclusion process, electrostatic field can be formed, and electronic cloud distortion above mud layer, can be formed, carry out adsorpting polymerization to the particulate matter in sewage, electric charge actual interacted sewage purification and filtration, the sewage after filtration rises to water outlet and completes water outlet.
The process that oily(waste)water integral purifier is purified waste water is, sewage lagoon sewage is by adding sterilant, remove bacterium in water, stabilizing water quality, then flocculation agent is added, the oil in sewage, suspended particle, oil in water emulsion mixture adsorbs, impurity absorption in sewage is formed the floc sedimentation of bulk, then add coagulant aids flco is increased the weight of, make sewage after entering oily(waste)water integral purifier, advance in the direction predetermined according to water trap, enter reaction cabin, mud discharging device is provided with bottom reaction cabin, by a small amount of spoil disposal, form downward gravity, mud is due to own wt, carry out mud-water separation, mud is made up of the impurity in medicament and sewage, mud layer is upwards in process, above reaction cabin, outlet can be arranged the sewage in rotation and be formed microelectronics cloud filtering layer, when mud enters into microelectronics cloud filtering layer time, mud is in continuous exclusion process, electrostatic field can be formed, and electronic cloud distortion above mud layer, can be formed, adsorpting polymerization is carried out to the particulate matter in sewage, electronic cloud filters the gravitation deriving from moment of dipole generation and comprises electric charge, dipole and its interaction of quadrupole moment are pressed 1/kT power exponent by Boltzmann weighting factor and are launched, electric charge actual interacted sewage purification and filtration, sewage after filtration rises to water outlet, complete water outlet.
Impurity in sewage can all adsorb by described microelectronics filtering layer, the oil of 99% also can adsorb, remaining a small amount of oil bloom upwards always, the gravity principle that water leg utilizes, oil bloom float, water outlet pipeline can not be entered, oil bloom rise always, rise to oil trap, regular discharge, approximately monthly oil extraction once, microelectronics cloud filtering layer is due to medicament, mud, sump oil forms, in operational process, reaction cabin discharges a part, equipment is stopped transport and is discharged major part, device start, automatic formation, the distance of reaction cabin distance set tank, it is exactly the amount of water outlet, the microelectronics filtering layer formation time of reaction cabin is after device start about 15 minutes, and the distance of water leg and reaction cabin is large, there is the water discharging time of 2 hours.
Index contrast before and after sewage disposal:
To those skilled in the art, obviously the invention is not restricted to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present invention or essential characteristic, the present invention can be realized in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present invention is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the present invention.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this specification sheets is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of specification sheets is only for clarity sake, those skilled in the art should by specification sheets integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (4)
1. an oily(waste)water integral purifier, this cleaner is tank structure, it is characterized in that: the top of described cleaner is provided with water leg (6) and oil trap (7), the position of oil trap (7) is higher than water leg (6), the middle part of described cleaner is reaction cabin (5), export above reaction cabin and connect water leg (6) and oil trap (7) respectively, sewage water inlet pipe (1) and shore pipe (3) is provided with in the side of cleaner, sewage water inlet pipe stretches into cleaner and is connected with reaction cabin (5), shore pipe (3) is provided with bottom reaction cabin, the outlet of shore pipe (3) is outside tank body, silt after mud-water separation is discharged by shore pipe (3), upflow tube (4) and rising pipe (2) is provided with in the side of cleaner, in tank body, water level begins through upflow tube (4) water outlet after exceeding oil trap, described water leg (6) connects rising pipe (2), water leg (6), two pipelines that oil trap (7) connects are directly through reaction cabin (5), in the bottom water outlet of tank body.
2. a kind of oily(waste)water integral purifier according to claim 1, it is characterized in that: above described reaction cabin, outlet can be arranged the sewage in rotation and be formed microelectronics cloud filtering layer, when mud enters into microelectronics cloud filtering layer time, mud is in continuous exclusion process, electrostatic field can be formed, and electronic cloud distortion above mud layer, can be formed, adsorpting polymerization is carried out to the particulate matter in sewage, electric charge actual interacted sewage purification and filtration, the sewage after filtration rises to water outlet and completes water outlet.
3. the process that a kind of oily(waste)water integral purifier according to claim 1 and 2 is purified waste water is, sewage lagoon sewage is by adding sterilant, remove bacterium in water, stabilizing water quality, then flocculation agent is added, the oil in sewage, suspended particle, oil in water emulsion mixture adsorbs, impurity absorption in sewage is formed the floc sedimentation of bulk, then add coagulant aids flco is increased the weight of, make sewage after entering oily(waste)water integral purifier, advance in the direction predetermined according to water trap, enter reaction cabin, mud discharging device is provided with bottom reaction cabin, by a small amount of spoil disposal, form downward gravity, mud is due to own wt, carry out mud-water separation, mud is made up of the impurity in medicament and sewage, mud layer is upwards in process, above reaction cabin, outlet can be arranged the sewage in rotation and be formed microelectronics cloud filtering layer, when mud enters into microelectronics cloud filtering layer time, mud is in continuous exclusion process, electrostatic field can be formed, and electronic cloud distortion above mud layer, can be formed, adsorpting polymerization is carried out to the particulate matter in sewage, electronic cloud filters the gravitation deriving from moment of dipole generation and comprises electric charge, dipole and its interaction of quadrupole moment are pressed 1/kT power exponent by Boltzmann weighting factor and are launched, electric charge actual interacted sewage purification and filtration, sewage after filtration rises to water outlet, complete water outlet.
4. the process of a kind of oily(waste)water integral purifier according to claim 3, it is characterized in that: the impurity in sewage can all adsorb by described microelectronics filtering layer, the oil of 99% also can adsorb, remaining a small amount of oil bloom upwards always, the gravity principle that water leg utilizes, oil bloom float, water outlet pipeline can not be entered, oil bloom rise always, rise to oil trap, regular discharge, approximately monthly oil extraction once, microelectronics cloud filtering layer is due to medicament, mud, sump oil forms, in operational process, reaction cabin discharges a part, equipment is stopped transport and is discharged major part, device start, automatic formation, the distance of reaction cabin distance set tank, it is exactly the amount of water outlet, the microelectronics filtering layer formation time of reaction cabin is after device start about 15 minutes, and the distance of water leg and reaction cabin is large, there is the water discharging time of 2 hours.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510938908.1A CN105384299A (en) | 2015-12-16 | 2015-12-16 | Oil-containing sewage integrated purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510938908.1A CN105384299A (en) | 2015-12-16 | 2015-12-16 | Oil-containing sewage integrated purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105384299A true CN105384299A (en) | 2016-03-09 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510938908.1A Pending CN105384299A (en) | 2015-12-16 | 2015-12-16 | Oil-containing sewage integrated purifier |
Country Status (1)
| Country | Link |
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| CN (1) | CN105384299A (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2581434Y (en) * | 2002-11-26 | 2003-10-22 | 李洪祥 | Sewage treating pot |
| US7172699B1 (en) * | 2004-10-13 | 2007-02-06 | Eimco Water Technologies Llc | Energy efficient wastewater treatment for nitrogen and phosphorus removal |
| CN201108756Y (en) * | 2007-09-24 | 2008-09-03 | 王秀君 | Combined separation facility for oily sewage |
| CN201240881Y (en) * | 2008-07-17 | 2009-05-20 | 李继凤 | Aeration treatment apparatus for oilfield oil-contaminated water |
| CN101723554A (en) * | 2009-12-31 | 2010-06-09 | 华南理工大学 | Chemical fertilizer waste water treatment method |
| CN202945071U (en) * | 2012-12-19 | 2013-05-22 | 大庆高新区百世环保科技开发有限公司 | Oil field injected water secondary pollution comprehensive control device |
| CN103241904A (en) * | 2013-05-24 | 2013-08-14 | 郑州大学 | Multi-point water inlet aeration anoxic-aerobic high-efficient nitrogen and phosphorus removal method |
| CN103739045A (en) * | 2013-11-29 | 2014-04-23 | 陈大矛 | Equipment and method for treating industrial wastewater through positive-negative polarity electrostatic absorption method |
-
2015
- 2015-12-16 CN CN201510938908.1A patent/CN105384299A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2581434Y (en) * | 2002-11-26 | 2003-10-22 | 李洪祥 | Sewage treating pot |
| US7172699B1 (en) * | 2004-10-13 | 2007-02-06 | Eimco Water Technologies Llc | Energy efficient wastewater treatment for nitrogen and phosphorus removal |
| CN201108756Y (en) * | 2007-09-24 | 2008-09-03 | 王秀君 | Combined separation facility for oily sewage |
| CN201240881Y (en) * | 2008-07-17 | 2009-05-20 | 李继凤 | Aeration treatment apparatus for oilfield oil-contaminated water |
| CN101723554A (en) * | 2009-12-31 | 2010-06-09 | 华南理工大学 | Chemical fertilizer waste water treatment method |
| CN202945071U (en) * | 2012-12-19 | 2013-05-22 | 大庆高新区百世环保科技开发有限公司 | Oil field injected water secondary pollution comprehensive control device |
| CN103241904A (en) * | 2013-05-24 | 2013-08-14 | 郑州大学 | Multi-point water inlet aeration anoxic-aerobic high-efficient nitrogen and phosphorus removal method |
| CN103739045A (en) * | 2013-11-29 | 2014-04-23 | 陈大矛 | Equipment and method for treating industrial wastewater through positive-negative polarity electrostatic absorption method |
Non-Patent Citations (1)
| Title |
|---|
| 段钧元等: "絮凝剂强化微电解法处理罗丹明B废水的研究", 《化工技术与开发》 * |
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| PB01 | Publication | ||
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Application publication date: 20160309 |