CN105621723A - Petroleum sewage treatment method - Google Patents
Petroleum sewage treatment method Download PDFInfo
- Publication number
- CN105621723A CN105621723A CN201410603799.3A CN201410603799A CN105621723A CN 105621723 A CN105621723 A CN 105621723A CN 201410603799 A CN201410603799 A CN 201410603799A CN 105621723 A CN105621723 A CN 105621723A
- Authority
- CN
- China
- Prior art keywords
- sewage
- waste water
- flocculant
- processing
- petroleum
- 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
- 239000010865 sewage Substances 0.000 title claims abstract description 48
- 238000000034 method Methods 0.000 title claims abstract description 18
- 239000003208 petroleum Substances 0.000 title claims abstract description 17
- 239000002351 wastewater Substances 0.000 claims abstract description 35
- 238000001914 filtration Methods 0.000 claims abstract description 21
- 239000012535 impurity Substances 0.000 claims abstract description 16
- 239000002699 waste material Substances 0.000 claims abstract description 15
- 239000000126 substance Substances 0.000 claims abstract description 13
- 239000007787 solid Substances 0.000 claims abstract description 7
- 238000003672 processing method Methods 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 13
- 239000000701 coagulant Substances 0.000 claims description 12
- 239000000839 emulsion Substances 0.000 claims description 6
- 238000004062 sedimentation Methods 0.000 claims description 6
- 239000006004 Quartz sand Substances 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 229920002472 Starch Polymers 0.000 claims description 4
- 159000000013 aluminium salts Chemical class 0.000 claims description 4
- 229910000329 aluminium sulfate Inorganic materials 0.000 claims description 4
- 239000003245 coal Substances 0.000 claims description 4
- 229920000620 organic polymer Polymers 0.000 claims description 4
- 229920002401 polyacrylamide Polymers 0.000 claims description 4
- 235000019698 starch Nutrition 0.000 claims description 4
- 239000008107 starch Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 8
- 239000003795 chemical substances by application Substances 0.000 abstract description 3
- 230000015271 coagulation Effects 0.000 abstract 1
- 238000005345 coagulation Methods 0.000 abstract 1
- 238000005189 flocculation Methods 0.000 abstract 1
- 230000016615 flocculation Effects 0.000 abstract 1
- 238000001556 precipitation Methods 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 22
- 239000010779 crude oil Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000053 physical method Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a petroleum sewage treatment method. The method is specifically implemented with the following steps: sewage is introduced into a precipitation filtration tank, such that preliminary filtration is carried out, and various solid impurities in the sewage are removed; the treated sewage is introduced into a coarse-graining treatment tank where waste oil contained in the sewage is removed through coarse-graining treatment; a flocculation agent is added into treated sewage; flocs with absorbed waste oil are moved through filtration; wastewater is discharged into a chemical treatment tank; a coagulation agent is added, such that emulsified oil in the oil-containing wastewater is removed; and the treated wastewater is delivered to departments adopting the recycled water through pipes. With the petroleum sewage treatment method provided by the invention, problems of low efficiency and high treatment cost of petroleum sewage treatment methods in prior arts are solved.
Description
Technical field
The invention belongs to sewage water treatment method technical field, relate to a kind of petroleum waste water processing method.
Background technology
Oil field generally all adopts the development scheme of water filling, particularly much has been enter into the oil field of middle and late stage mining phase, and crude oil water content is high, causes oil recovery treatment more difficult. The comparison of ingredients contained in oil extraction-generated waste water is complicated, typically contain crude oil, Organic substance, inorganic salt, salt, microorganism etc., its water temperature, salinity, antibacterial amount are higher, and remaining has many impurity, traditional Technology to be extremely difficult to the requirement that oilfield produced water processes. The dosing of the oil recovery treatment adopted at present is very big, causes that medicament expense increases, considerably increases the cost in oil field, reduce economic benefit, develop efficiently, the task of the sewage-treating agent of low cost extremely urgent.
Summary of the invention
It is an object of the invention to provide a kind of petroleum waste water processing method, solve prior art petroleum waste water processing method efficiency low, the problem that processing cost is high.
The technical solution adopted in the present invention is, a kind of petroleum waste water processing method, specifically implements according to following steps:
Step 1, introduces sedimentation and filtration ditch by sewage, carries out preliminary filtration, thus the various solid impurities removed in sewage.
Step 2, is introduced coarse process pond by the sewage after processing in step 1, is processed by coarse and remove waste oil contained in sewage,
Step 3, to adding flocculant in the sewage after processing in step 2, wherein flocculant is mainly organic polymer flocculant and the big class of inorganic flocculant two. The flocculant thrown in and the mass ratio of sewage are 1:50��100, then pass through and filter the flco removal that will be adsorbed with waste oil;
Step 4, enters chemical treatment pool by the waste water after processing in step 3, gives and wherein add coagulant, thus the oil emulsion removed in oily waste water;
Step 5, is delivered to, by the waste water after processing in step 4, the department that can reuse by pipeline.
The feature of the present invention also resides in,
Wherein, filtering ponds are for being divided into multilamellar, and the diameter of every layer of filtrable impurity is different.
Wherein, the coarse material of use can be mineral-type materials, such as quartz sand or coal grain. Can also be Organic substance, such as lipophile material.
Wherein, the coagulant of use is aluminium salt, polyacrylamide or graft starch.
The invention has the beneficial effects as follows, select and be reasonably scheduled that multiple processing method, in conjunction with using these processing methods, make the process of petroleum waste water more efficiently, not only efficiency is fast at high speed, and its effect removing dirty impurities in water is also fine, the physical method that first use cost is relatively low, then re-uses the method needing to add chemical substance, and such arrangement can effectively reduce the cost processing sewage.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the present invention is described in detail.
One petroleum waste water processing method of the present invention, specifically implements according to following steps:
Step 1, introduces sedimentation and filtration ditch by sewage, carries out preliminary filtration, thus the various solid impurities removed in sewage.
Filtering ponds therein are for being divided into multilamellar, and the diameter of every layer of filtrable impurity is different.
Step 2, is introduced coarse process pond by the sewage after processing in step 1, is processed by coarse and remove waste oil contained in sewage, and the coarse material wherein used can be mineral-type materials, such as quartz sand or coal grain. Can also be Organic substance, such as lipophile material.
Step 3, to adding flocculant in the sewage after processing in step 2, wherein flocculant is mainly organic polymer flocculant and the big class of inorganic flocculant two. The flocculant thrown in and the mass ratio of sewage are 1:50��100, and much more especially the consumption of this method use flocculant is less, because in step above, has eliminated the waste oil of part, it is possible to need not flocculant. Then pass through to filter and the flco being adsorbed with waste oil is removed;
Step 4, enters chemical treatment pool by the waste water after processing in step 3, gives and wherein add coagulant, thus the oil emulsion removed in oily waste water; The coagulant used is aluminium salt, polyacrylamide or graft starch.
Step 5, is delivered to, by the waste water after processing in step 4, the department that can reuse by pipeline.
The petroleum waste water processing method of the present invention, select and be reasonably scheduled that multiple processing method, in conjunction with using these processing methods, make the process of petroleum waste water more efficiently, not only efficiency is fast at high speed, and its effect removing dirty impurities in water is also fine, the physical method that first use cost is relatively low, then re-uses the method needing to add chemical substance, and such arrangement can effectively reduce the cost processing sewage.
Embodiment 1
Step 1, introduces sedimentation and filtration ditch by sewage, carries out preliminary filtration, thus the various solid impurities removed in sewage.
Filtering ponds therein are for being divided into multilamellar, and the diameter of every layer of filtrable impurity is different.
Step 2, is introduced coarse process pond by the sewage after processing in step 1, is processed by coarse and remove waste oil contained in sewage, and the coarse material wherein used is quartz sand;
Step 3, to adding flocculant in the sewage after processing in step 2, wherein flocculant is organic polymer flocculant, and the flocculant of input and the mass ratio of sewage are 1:50, then passes through to filter and is removed by the flco being adsorbed with waste oil;
Step 4, enters chemical treatment pool by the waste water after processing in step 3, gives and wherein add coagulant, thus the oil emulsion removed in oily waste water; The coagulant used is aluminium salt.
Step 5, is delivered to, by the waste water after processing in step 4, the department that can reuse by pipeline.
Embodiment 2
Step 1, introduces sedimentation and filtration ditch by sewage, carries out preliminary filtration, thus the various solid impurities removed in sewage.
Filtering ponds therein are for being divided into multilamellar, and the diameter of every layer of filtrable impurity is different.
Step 2, is introduced coarse process pond by the sewage after processing in step 1, is processed by coarse and remove waste oil contained in sewage, and the coarse material wherein used is person's coal grain.
Step 3, to adding flocculant in the sewage after processing in step 2, wherein flocculant is the inorganic big class of flocculant two. The flocculant thrown in and the mass ratio of sewage are 1:100, then pass through and filter the flco removal that will be adsorbed with waste oil;
Step 4, enters chemical treatment pool by the waste water after processing in step 3, gives and wherein add coagulant, thus the oil emulsion removed in oily waste water; The coagulant used is polyacrylamide;
Step 5, is delivered to, by the waste water after processing in step 4, the department that can reuse by pipeline.
Embodiment 3
Step 1, introduces sedimentation and filtration ditch by sewage, carries out preliminary filtration, thus the various solid impurities removed in sewage;
Filtering ponds therein are for being divided into multilamellar, and the diameter of every layer of filtrable impurity is different;
Step 2, is introduced coarse process pond by the sewage after processing in step 1, is processed by coarse and remove waste oil contained in sewage, and the coarse material wherein used is lipophile material;
Step 3, to adding flocculant in the sewage after processing in step 2, wherein flocculant is mainly inorganic flocculant, and the flocculant of input and the mass ratio of sewage are 1:70, then passes through to filter and is removed by the flco being adsorbed with waste oil;
Step 4, enters chemical treatment pool by the waste water after processing in step 3, gives and wherein add coagulant, thus the oil emulsion removed in oily waste water; The coagulant used is graft starch;
Step 5, is delivered to, by the waste water after processing in step 4, the department that can reuse by pipeline.
Claims (4)
1. a petroleum waste water processing method, it is characterised in that specifically implement according to following steps:
Step 1, introduces sedimentation and filtration ditch by sewage, carries out preliminary filtration, thus the various solid impurities removed in sewage;
Step 2, is introduced coarse process pond by the sewage after processing in step 1, is processed by coarse and remove waste oil contained in sewage,
Step 3, to adding flocculant in the sewage after processing in step 2, wherein flocculant is mainly organic polymer flocculant and the big class of inorganic flocculant two; The flocculant thrown in and the mass ratio of sewage are 1:50��100, then pass through and filter the flco removal that will be adsorbed with waste oil;
Step 4, enters chemical treatment pool by the waste water after processing in step 3, gives and wherein add coagulant, thus the oil emulsion removed in oily waste water;
Step 5, is delivered to, by the waste water after processing in step 4, the department that can reuse by pipeline.
2. petroleum waste water processing method according to claim 1, it is characterised in that the filtering ponds in described step 1 are for being divided into multilamellar, and the diameter of every layer of filtrable impurity is different.
3. petroleum waste water processing method according to claim 1, it is characterised in that the coarse material used in described step 2 can be mineral-type materials, such as quartz sand or coal grain, it is also possible to be Organic substance, such as lipophile material.
4. petroleum waste water processing method according to claim 1, it is characterised in that the coagulant used in described step 4 is aluminium salt, polyacrylamide or graft starch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410603799.3A CN105621723A (en) | 2014-10-30 | 2014-10-30 | Petroleum sewage treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410603799.3A CN105621723A (en) | 2014-10-30 | 2014-10-30 | Petroleum sewage treatment method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105621723A true CN105621723A (en) | 2016-06-01 |
Family
ID=56037130
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410603799.3A Pending CN105621723A (en) | 2014-10-30 | 2014-10-30 | Petroleum sewage treatment method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105621723A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106905993A (en) * | 2017-03-24 | 2017-06-30 | 诗茵（海南）环保科技有限公司 | A kind of environment protection treating technique of mineral oil discarded object |
| CN109761451A (en) * | 2019-03-19 | 2019-05-17 | 广西科学院 | A kind of treatment method for oil polluted water body containing algae |
| CN116444103A (en) * | 2023-06-12 | 2023-07-18 | 扬州澄露环境工程有限公司 | Vertical oil-water separator |
-
2014
- 2014-10-30 CN CN201410603799.3A patent/CN105621723A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106905993A (en) * | 2017-03-24 | 2017-06-30 | 诗茵（海南）环保科技有限公司 | A kind of environment protection treating technique of mineral oil discarded object |
| CN109761451A (en) * | 2019-03-19 | 2019-05-17 | 广西科学院 | A kind of treatment method for oil polluted water body containing algae |
| CN116444103A (en) * | 2023-06-12 | 2023-07-18 | 扬州澄露环境工程有限公司 | Vertical oil-water separator |
| CN116444103B (en) * | 2023-06-12 | 2023-09-26 | 扬州澄露环境工程有限公司 | Vertical oil-water separator |
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| C06 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160601 |
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| WD01 | Invention patent application deemed withdrawn after publication |