CN102583674A - Integrated oily mud wastewater pipe bundle coagulation and separation reactor - Google Patents
Integrated oily mud wastewater pipe bundle coagulation and separation reactor Download PDFInfo
- Publication number
- CN102583674A CN102583674A CN2012100520399A CN201210052039A CN102583674A CN 102583674 A CN102583674 A CN 102583674A CN 2012100520399 A CN2012100520399 A CN 2012100520399A CN 201210052039 A CN201210052039 A CN 201210052039A CN 102583674 A CN102583674 A CN 102583674A
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- water
- pipe
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- 238000000926 separation method Methods 0.000 title claims abstract description 20
- 239000002351 wastewater Substances 0.000 title abstract description 12
- 238000005345 coagulation Methods 0.000 title abstract description 5
- 230000015271 coagulation Effects 0.000 title abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 238000003860 storage Methods 0.000 claims abstract description 13
- 238000010926 purge Methods 0.000 claims abstract description 11
- 238000009826 distribution Methods 0.000 claims abstract description 10
- 239000000126 substance Substances 0.000 claims abstract description 6
- 239000002699 waste material Substances 0.000 claims description 13
- 238000005054 agglomeration Methods 0.000 claims description 12
- 230000002776 aggregation Effects 0.000 claims description 12
- 238000007599 discharging Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 230000000630 rising effect Effects 0.000 claims description 4
- 239000011152 fibreglass Substances 0.000 claims description 2
- 230000003319 supportive effect Effects 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 5
- 238000011084 recovery Methods 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 239000004058 oil shale Substances 0.000 abstract description 2
- 239000000835 fiber Substances 0.000 abstract 2
- 238000005065 mining Methods 0.000 abstract 1
- 238000005192 partition Methods 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 24
- 239000002245 particle Substances 0.000 description 14
- 230000008021 deposition Effects 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 5
- 238000004581 coalescence Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000005484 gravity Effects 0.000 description 3
- 230000002000 scavenging effect Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
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Abstract
The invention relates to an integrated oil-contained wastewater pipe bundle coagulation and separation reactor which comprises a reactor main body, a water inlet pipe, a chemical feed pipe, a water outlet pipe, an emptying pipe, an oil recovering pipe and an air purging pipe are arranged on the main body, and a support is used for supporting the main body. A mud storage region, a water baffle plate, a pipe bundle settling region, a fiber bundle coagulation and coarse graining region, a water distribution plate and the like are mainly installed inside the reactor, the reactor is obliquely installed on the support, the mud storage region is located at the lower part inside the reactor main body, the water baffle plate, a pipe bundle, a water partition plate, the pipe bundle settling region and the fiber bundle coagulation and coarse graining region are located at the middle part, and the water distribution plate and an oil separation plate at the upper part form an oil and water separation region. The reactor has good removal and recovery effect on wastewater containing mud and oil, low energy consumption and small land coverage and is flexible to disassemble, assemble and transport, the mud removal rate can reach more than 95% for oil shale washing wastewater and oil field mining wastewater, the oil recovery rate can reach 90%, the grain size of oil in drained water is smaller than 10 mum, and the mud content is smaller than 10%.
Description
Technical field
The invention belongs to the technology for treating industrial waste water field; Relate to a kind of greasy filth waste pipe bundle agglomeration separation reactor drum that contains, the present invention is specially adapted to aspects such as field oil-containings such as oil production, chemical industry, iron and steel, electric power, the removal of silt particle trade effluent silt particle, recovery of oil utilization.
Background technology:
Containing greasy filth waste pipe bundle agglomeration separation reactor drum is that a kind of waste water silt particle that on sloping plate deposition and cohesion adsorption technology basis, develops is removed, recovery of oil utilizes integrated reactor.
Traditional silt particle and general separate treatment of oily waste water of containing.Wherein " the shallow layer precipitating principle adopts advection, erects stream or inclined-plate clarifying basin removal silt particle, and oil removing is mainly adopted and condensed absorption, air-float technology processing except that silt particle mainly utilizes.Mainly contain following shortcoming:
(1) oil slick is received oil through scraper plate, and greasy filth mixes, and separates not thoroughly, influences the refiltered oil quality;
(2) rely on settling tank pressure spoil disposal or pump spoil disposal, spoil disposal is untimely thoroughly, often causes sludge bulking;
(3) rely on dosing pond or dosing tank dosing, water distribution is uneven, needs to increase mechanical stirring or line mixer raising coagulation effect, increases cost;
(4) generally adopt civil engineering structure, the facility floor space is big, and is not removable.
Above drawbacks limit promoting the use of of conventional process device.
Summary of the invention
The present invention fully utilizes the principle that the baffling collision mixes dosing, tube bank deposition, cohesion coarse, gravity buoyancy oil removal; Propose silt particle in a kind of efficient removal waste water and reclaim the integrated greasy filth waste pipe bundle agglomeration separation reactor drum that contains of oils; Multiple removal greasy filth technology is integrated, have that greasy filth different process branch matter is separated, aggegation oil and water separation bygranulation and gravity buoyancy oil removal combine, remove efficient height, occupation of land less, integrated advantage such as easy to install.
The present invention realizes through following technical scheme: the integrated greasy filth waste pipe bundle agglomeration separation reactor drum that contains; Comprise reactor body; Be arranged at water inlet pipe, chemical feed pipe, rising pipe, shore pipe, collection tube, the air purge pipe on the main body and be used for the support of supportive body, inside reactor mainly contains storage mud district, water eliminator, tube bank settling region, fibrous bundle cohesion coarse district, water distribution board etc.
Reactor drum tilts rack-mount, and reactor body inside comprises the storage mud district that is positioned at the bottom again, the water eliminator at middle part, tube bank, water-stop sheet, tube bank settling region and fibrous bundle cohesion coarse district, the oily water separation district that the water distribution board on top, oil dividing plate constitute.
Said reactor body be shaped as round shape, tilt to be installed on the support.
Described storage mud district also is provided with the helical feed mud discharging device.
Glass reinforced plastic or other material smooth pipes are installed in said tube bank settling region.
Said fibrous bundle cohesion coarse district is installed between the slit of cylindrical shell and tube bank.
Said air purge pipe regularly purges tube bank district silt.
Storage mud district, bottom is mainly used in the settlement on storage silt particle, online spiral sludge discharge; Water eliminator, water-stop sheet, make into water and tube bank each other collision be beneficial to dosing and mix, the precipitation process of silt is accomplished in the tube bank settling region, fibrous bundle cohesion coarse district mainly accomplishes profit gathering coarse particles and divides and leave.
The main characteristic of this reactor drum is:
Reactor monolith tilt to be installed, and intakes and restrains repeatedly the mixed effect that the baffling collision improves medicine and water; The tube bank deposition is removed silt, and cohesion coarse district makes little oil droplet aggregate into larger oil droplet, and the larger oil droplet come-up realizes oily water separation; Regularly air purge tube bank district silt condenses the oil droplet of coarse district's coalescence with fibrous bundle, makes the reactor drum can long-play.
This reactor drum has following advantage:
(1) baffling collision mixing dosing, tube bank deposition, cohesion coarse, gravity buoyancy oil removing combine, and the removal efficient of greasy filth is high;
(2) the utilization tube bank is constantly bumped to change the line of production with water and is given birth to turbulent flow raising mixed effect, need not extra static mixer,
(3) equipment is integrated, and floor space is little, easy accessibility;
(4) the pressurized air scavenging duct regularly purges the silt in the tube bank, can guarantee the reactor drum life-time service.
The present invention is good for containing silt particle and oils waste water removal recovering effect, and energy consumption is low, occupation of land is little, and dismounting is moved flexibly; Adopt notes waste water for oil shale washes and oil field, the silt particle clearance can reach more than 95%, and oil-collecting ratio can reach 90%; Oil-containing particle diameter in the draining < 10um, silt content < 10%.
Description of drawings
Fig. 1 is a structural representation of the present invention;
Fig. 2 mixes synoptic diagram for water inlet with the tube bank collision;
Fig. 3 is tube bank settling region and fibrous bundle cohesion coarse zone position synoptic diagram.
Among the figure: 1, water inlet pipe, 2, chemical feed pipe, 3, water shoot, 4, evacuated tube; 5, collection tube, 6, the pressurized air scavenging duct, 7, reactor body, 7a, storage mud district; 7b, helical feed mud discharging device, 7c, water eliminator, 7d, tube bank settling region, 7e, water distribution board; 7f, fibrous bundle cohesion coarse district, 7g, support, 7h, water-stop sheet.
Embodiment
Specify the present invention below in conjunction with accompanying drawing.
The integrated greasy filth waste pipe bundle agglomeration separation reactor drum that contains comprises reactor body 7, is arranged at water inlet pipe 1, chemical feed pipe 2, rising pipe 3, evacuated tube 4, collection tube 5, pressurized air scavenging duct 6 on the main body; Inside reactor mainly contains storage mud district 7a, helical feed mud discharging device 7b, water eliminator 7c, tube bank settling region 7d; Water distribution board 7e; Fibrous bundle cohesion coarse district 7f, support 7g, water-stop sheet 7h, as shown in Figure 1.
Concrete principle of work is following; Containing silt particle and oily waste water gets in the reactor body 7 through water inlet pipe 1; Sewage is blocked by two ends water eliminator 7c up and down, can only get into tube bank settling region 7d by the perforate of tube bank settling region 7d sidewall along water-stop sheet-7h, during with constantly collision of tube bank; As shown in Figure 2, thus the dosing mixing efficiency improved owing to turbulent phenomenon constantly occurs; Waste water got into tube bank settling region 7d after dosing mixed, and silt particle has mainly utilized lamina flow principle because gravitational settling in tube bank, is restrained deposition in the process of stream waterborne, shortened the solids precipitation distance, thereby shortened the ST, has improved sediment deposition efficient; Sewage gets into fibrous bundle cohesion coarse district 7f after by water distribution board 7e baffle behind the sediment deposition, and is as shown in Figure 3, accomplishes profit and assemble coarse particles and divide and leave; The isolating principle of cohesion coarse is a characteristic of utilizing profit two relative coalescence material avidity to differ greatly, and when oily(waste)water passed through lipophilic coalescence material, tiny elaioleucite was trapped and is attached in material surface or the hole in the water; The oil droplet that is trapped, expansion wetting at material surface; Further with on every side elaioleucite collision coalescence, oil droplet increases gradually, Gu when the buoyancy of oil droplet greater than oil---between attachment energy the time; Elaioleucite just peels off from solid surface, and come-up is separated; The oil slick of come-up is stored in the reactor drum upper end, regularly discharges through collection tube, and rising pipe 3 flows out water from the bottom.Silt particle gets into bottom storage mud district 7a through the tube bank deposition, through the online discharging of helical feed mud discharging device 7b.Reactor drum regularly purges through the last silt of air purge pipe 6 pairs of tube banks settling region-7d, to guarantee the reactor drum life-time service.
Claims (6)
1. the integrated greasy filth waste pipe bundle agglomeration separation reactor drum that contains; Comprise reactor body (7); Be arranged at water inlet pipe (1), chemical feed pipe (2), rising pipe (3), evacuated tube (4), collection tube (5), the air purge pipe (6) on the main body (7) and be used for the support (7g) of supportive body (7); Inside reactor mainly contains storage mud district (7a), water eliminator (7c), tube bank settling region (7d), fibrous bundle cohesion coarse district (7f), water distribution board (7e) etc.; It is characterized in that: reactor drum tilts rack-mount; The inner storage mud district (7a) that is positioned at the bottom that comprises again of reactor body (7); The water eliminator (7c) at middle part, tube bank, water-stop sheet (7h), tube bank settling region (7d) and fibrous bundle cohesion coarse district (7f), the oily water separation district that the water distribution board on top (7e), oil dividing plate constitute.
2. the integrated greasy filth waste pipe bundle agglomeration separation reactor drum that contains according to claim 1 is characterized in that: said reactor body (7) be shaped as round shape, tilt to be installed on the support (7g).
3. the integrated greasy filth waste pipe bundle agglomeration separation reactor drum that contains according to claim 1, it is characterized in that: described storage mud district (7a) also is provided with helical feed mud discharging device (7b).
4. the integrated greasy filth waste pipe bundle agglomeration separation reactor drum that contains according to claim 1 is characterized in that: glass reinforced plastic or other material smooth pipes are installed in said tube bank settling region (7d).
5. the integrated greasy filth waste pipe bundle agglomeration separation reactor drum that contains according to claim 1 is characterized in that: said fibrous bundle cohesion coarse district (7f) is installed between the slit of cylindrical shell and tube bank.
6. the integrated greasy filth waste pipe bundle agglomeration separation reactor drum that contains according to claim 1 is characterized in that: said air purge pipe (6) regularly purges tube bank district silt.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201210052039 CN102583674B (en) | 2012-03-02 | 2012-03-02 | Integrated oily mud wastewater pipe bundle coagulation and separation reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201210052039 CN102583674B (en) | 2012-03-02 | 2012-03-02 | Integrated oily mud wastewater pipe bundle coagulation and separation reactor |
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| Publication Number | Publication Date |
|---|---|
| CN102583674A true CN102583674A (en) | 2012-07-18 |
| CN102583674B CN102583674B (en) | 2013-07-24 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201210052039 Active CN102583674B (en) | 2012-03-02 | 2012-03-02 | Integrated oily mud wastewater pipe bundle coagulation and separation reactor |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103274498A (en) * | 2013-06-20 | 2013-09-04 | 青岛科力源环境科技有限公司 | Oil-water separator |
| CN109911981A (en) * | 2019-03-01 | 2019-06-21 | 中国矿业大学 | A kind of coarse device for oily waste water treatment |
| CN114249446A (en) * | 2021-12-27 | 2022-03-29 | 华夏碧水环保科技有限公司 | Coal-based needle coke wastewater treatment system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0463199A (en) * | 1990-07-03 | 1992-02-28 | Tada Hideyo | Method and equipment for treating waste water |
| CN2213725Y (en) * | 1995-01-10 | 1995-11-29 | 易书盛 | Case type no-power dynamic oil-water separating device |
| CN1453227A (en) * | 2002-04-27 | 2003-11-05 | 中国科学院沈阳应用生态研究所 | Biochemical reactor for treating oil field sewage and its treating process |
| CN201043155Y (en) * | 2007-01-26 | 2008-04-02 | 万奥普（北京）石油工程技术开发研究院有限公司 | Ternary device for treatment of sewage of oil field |
| CN202529898U (en) * | 2012-03-02 | 2012-11-14 | 大连贝斯特环境工程设备有限公司 | Integrated condensation and separation reactor of waste water pipe bundle with oil sludge |
-
2012
- 2012-03-02 CN CN 201210052039 patent/CN102583674B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0463199A (en) * | 1990-07-03 | 1992-02-28 | Tada Hideyo | Method and equipment for treating waste water |
| CN2213725Y (en) * | 1995-01-10 | 1995-11-29 | 易书盛 | Case type no-power dynamic oil-water separating device |
| CN1453227A (en) * | 2002-04-27 | 2003-11-05 | 中国科学院沈阳应用生态研究所 | Biochemical reactor for treating oil field sewage and its treating process |
| CN201043155Y (en) * | 2007-01-26 | 2008-04-02 | 万奥普（北京）石油工程技术开发研究院有限公司 | Ternary device for treatment of sewage of oil field |
| CN202529898U (en) * | 2012-03-02 | 2012-11-14 | 大连贝斯特环境工程设备有限公司 | Integrated condensation and separation reactor of waste water pipe bundle with oil sludge |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103274498A (en) * | 2013-06-20 | 2013-09-04 | 青岛科力源环境科技有限公司 | Oil-water separator |
| CN103274498B (en) * | 2013-06-20 | 2014-07-30 | 刘同鑫 | Oil-water separator |
| CN109911981A (en) * | 2019-03-01 | 2019-06-21 | 中国矿业大学 | A kind of coarse device for oily waste water treatment |
| CN109911981B (en) * | 2019-03-01 | 2023-08-22 | 中国矿业大学 | Coarse graining device for oily sewage treatment |
| CN114249446A (en) * | 2021-12-27 | 2022-03-29 | 华夏碧水环保科技有限公司 | Coal-based needle coke wastewater treatment system |
| CN114249446B (en) * | 2021-12-27 | 2023-04-25 | 华夏碧水环保科技股份有限公司 | Coal-based needle coke wastewater treatment system |
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| Publication number | Publication date |
|---|---|
| CN102583674B (en) | 2013-07-24 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
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Denomination of invention: Integrated tube bundle coagulation separation reactor for oily sludge wastewater Effective date of registration: 20221212 Granted publication date: 20130724 Pledgee: Dalian Branch of Shanghai Pudong Development Bank Co.,Ltd. Pledgor: DALIAN BEST ENVIRONMENT EQUIPMENT Co.,Ltd. Registration number: Y2022980026415 |
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Date of cancellation: 20240103 Granted publication date: 20130724 Pledgee: Dalian Branch of Shanghai Pudong Development Bank Co.,Ltd. Pledgor: DALIAN BEST ENVIRONMENT EQUIPMENT Co.,Ltd. Registration number: Y2022980026415 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Integrated Oil Mud Wastewater Bundle Coagulation and Separation Reactor Granted publication date: 20130724 Pledgee: Dalian Branch of Shanghai Pudong Development Bank Co.,Ltd. Pledgor: DALIAN BEST ENVIRONMENT EQUIPMENT Co.,Ltd. Registration number: Y2024980001872 |