CN108439752A - A kind of silt particle separating and dehydrating integrated oil silt particle reduction device - Google Patents
A kind of silt particle separating and dehydrating integrated oil silt particle reduction device Download PDFInfo
- Publication number
- CN108439752A CN108439752A CN201810181025.4A CN201810181025A CN108439752A CN 108439752 A CN108439752 A CN 108439752A CN 201810181025 A CN201810181025 A CN 201810181025A CN 108439752 A CN108439752 A CN 108439752A
- Authority
- CN
- China
- Prior art keywords
- silt particle
- vibrating screen
- dewaterer
- phase outlet
- storage tank
- 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
- 239000002245 particle Substances 0.000 title claims abstract description 34
- 101100041681 Takifugu rubripes sand gene Proteins 0.000 claims abstract description 27
- 239000004576 sand Substances 0.000 claims abstract description 27
- 239000007788 liquid Substances 0.000 claims abstract description 10
- 239000007791 liquid phase Substances 0.000 claims abstract description 8
- 239000007790 solid phase Substances 0.000 claims abstract description 7
- 230000018044 dehydration Effects 0.000 claims description 3
- 238000006297 dehydration reaction Methods 0.000 claims description 3
- 238000004064 recycling Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- 238000010992 reflux Methods 0.000 claims 1
- 238000002347 injection Methods 0.000 abstract description 12
- 239000007924 injection Substances 0.000 abstract description 12
- 239000010802 sludge Substances 0.000 abstract description 7
- 238000000034 method Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/127—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/02—General arrangement of separating plant, e.g. flow sheets specially adapted for oil-sand, oil-chalk, oil-shales, ozokerite, bitumen, or the like
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/06—Sludge reduction, e.g. by lysis
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Geology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treatment Of Sludge (AREA)
Abstract
The present invention provides a kind of silt particle separating and dehydrating integrated oil silt particle reduction device, wherein the storage pool connects the liquid inlet of cyclone separator by pump and pipeline, it is provided with dosing mouth at the top of cyclone separator, it is connect with pharmacy jar, mud mouth in the middle part of cyclone separator connects storage basin, the sand export of bottom connects sand storage tank, storage basin is connect with vibrating screen, the liquid-phase outlet of vibrating screen connects dewaterer, solid-phase outlet connects sand storage tank, the solid-phase outlet of dewaterer is connect with sand storage tank, and liquid-phase outlet is back to storage pool；Vibrating screen and dewaterer are fixed on conveyer belt, and conveyer belt is fixed on above storage basin；Advantage is：Sludge grain size is efficiently separated, by size controlling within the scope of small particle, re-injection efficiency can be effectively improved, reduce re-injection cost.
Description
Technical field
The present invention relates to field of environment protection, and in particular to a kind of silt particle separating and dehydrating integrated oil silt particle reduction device.
Background technology
Oil sludge and sand profile control reinjection technique is a kind of processing and using the scientific method that develops simultaneously, it in line with " from stratum, also in
The thinking on stratum " is a kind of mode of effective solution oil sludge and sand outlet.But current sludge re-injection technique, not to sludge
Grain size is efficiently separated, by size controlling within the scope of small particle.But injected scheme after all stirrings is taken, when long
Between stratum permeability decline is be easy to cause after re-injection, re-injection pressure increases, re-injection is difficult, needs relatively frequently to replace and increase note mud
Well；Large-sized sand brings injection pump pump head and is seriously worn in sludge, needs to be replaced frequently pump head, reduces the use effect of pump
Rate increases operating cost.For such case, research and development have manufactured proprietary silt particle separating and dehydrating integrated oil silt particle decrement and have set
It is standby, it works for oil recovery factory's profile control re-injection, re-injection efficiency can be effectively improved, reduce re-injection cost.
Invention content
It is an object of the invention to solve the deficiencies in the prior art, and provide a kind of silt particle separating and dehydrating integration greasy filth
Sand reduction device.
The present invention new technical solution be：A kind of silt particle separating and dehydrating integrated oil silt particle reduction device, including eddy flow
Separator, vibrating screen, dewaterer, the storage pool connect the liquid inlet of cyclone separator, cyclonic separation by pump and pipeline
It is provided with dosing mouth at the top of device, is connect with pharmacy jar, the mud mouth in the middle part of cyclone separator connects storage basin, and the sand export of bottom connects
Sand storage tank is connect, storage basin is connect with vibrating screen, and the liquid-phase outlet of vibrating screen connects dewaterer, and solid-phase outlet connects sand storage tank, takes off
The solid-phase outlet of water dispenser is connect with sand storage tank, and liquid-phase outlet is back to storage pool；Vibrating screen and dewaterer are fixed on conveyer belt,
Conveyer belt is fixed on above storage basin.
It is controlled by automatic control device between each group subset.
The cyclone separator upper layer oil slick recycling, superfine mud liquid enter storage basin, and the big grain size silt particle in bottom enters storage
Sand pond, mixing grain size mud liquid enter vibrating screen.
The vibrating screen accurately sorts grain size,<30 μm enter storage basin；>30 μm enter dewaterer.
The dewaterer,>It is discharged into sand storage tank after 30 μm of silt particle dehydration.
The beneficial effects of the invention are as follows：Sludge grain size is efficiently separated, by size controlling in small particle range
It is interior, re-injection efficiency can be effectively improved, re-injection cost is reduced.
Description of the drawings
Fig. 1 is the structural diagram of the present invention.
Wherein, 1 is storage pool, and 2 be pharmacy jar, and 3 be cyclone separator, and 4 be vibrating screen, and 5 be dewaterer, and 6 be storage basin,
7 be conveyer belt, and 8 be sand storage tank, and 9 be pump.
Specific implementation mode
The present invention will be further described below in conjunction with the accompanying drawings.
A kind of silt particle separating and dehydrating integrated oil silt particle reduction device, including cyclone separator 3, vibrating screen 4, dewaterer 5,
The storage pool 1 connects the liquid inlet of cyclone separator 3 by pump 9 and pipeline, and 3 top of cyclone separator is provided with dosing mouth,
It is connect with pharmacy jar 2, the mud mouth at 3 middle part of cyclone separator connects storage basin 6, and the sand export of bottom connects sand storage tank 8, stores up mud
Pond 6 is connect with vibrating screen 4, and the liquid-phase outlet of vibrating screen 4 connects dewaterer 5, and solid-phase outlet connects sand storage tank 8, and dewaterer 5 is consolidated
Mutually outlet is connect with sand storage tank 8, and liquid-phase outlet is back to storage pool 1；Vibrating screen 4 and dewaterer 5 are fixed on conveyer belt 7, are passed
Band 7 is sent to be fixed on 6 top of storage basin.
It is controlled by automatic control device between each group subset.
The 3 upper layer oil slick recycling of cyclone separator, superfine mud liquid enter storage basin 6, and the big grain size silt particle in bottom enters
Sand storage tank 8, mixing grain size mud liquid enter vibrating screen 4.
The vibrating screen 4 accurately sorts grain size,<30 μm enter storage basin 6；>30 μm enter dewaterer 5.
The dewaterer 5,>It is discharged into sand storage tank 8 after 30 μm of silt particle dehydration.
Claims (5)
1. a kind of silt particle separating and dehydrating integrated oil silt particle reduction device, including cyclone separator（3）, vibrating screen（4）, dewaterer
（5）, it is characterised in that：The storage pool（1）Pass through pump（9）And pipeline connects cyclone separator（3）Liquid inlet, eddy flow point
From device（3）Top is provided with dosing mouth, with pharmacy jar（2）Connection, cyclone separator（3）The mud mouth at middle part connects storage basin（6）,
The sand export of bottom connects sand storage tank（8）, storage basin（6）With vibrating screen（4）Connection, vibrating screen（4）Liquid-phase outlet connection it is de-
Water dispenser（5）, solid-phase outlet connection sand storage tank（8）, dewaterer（5）Solid-phase outlet and sand storage tank（8）Connection, liquid-phase outlet reflux
To storage pool（1）；Vibrating screen（4）And dewaterer（5）It is fixed on conveyer belt（7）On, conveyer belt（7）It is fixed on storage basin（6）On
Side.
2. a kind of silt particle separating and dehydrating integrated oil silt particle reduction device according to claim 1, it is characterised in that：It is described
Each group subset between controlled by automatic control device.
3. a kind of silt particle separating and dehydrating integrated oil silt particle reduction device according to claim 1, it is characterised in that：It is described
Cyclone separator（3）Upper layer oil slick recycling, superfine mud liquid enter storage basin（6）, the big grain size silt particle in bottom enters sand storage tank
（8）, mix grain size mud liquid and enter vibrating screen（4）.
4. a kind of silt particle separating and dehydrating integrated oil silt particle reduction device according to claim 1, it is characterised in that：It is described
Vibrating screen（4）Accurate sorting grain size,<30 μm enter storage basin（6）；>30 μm enter dewaterer（5）.
5. a kind of silt particle separating and dehydrating integrated oil silt particle reduction device according to claim 1, it is characterised in that：It is described
Dewaterer（5）,>It is discharged into sand storage tank after 30 μm of silt particle dehydration（8）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810181025.4A CN108439752A (en) | 2018-03-06 | 2018-03-06 | A kind of silt particle separating and dehydrating integrated oil silt particle reduction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810181025.4A CN108439752A (en) | 2018-03-06 | 2018-03-06 | A kind of silt particle separating and dehydrating integrated oil silt particle reduction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108439752A true CN108439752A (en) | 2018-08-24 |
Family
ID=63193585
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810181025.4A Pending CN108439752A (en) | 2018-03-06 | 2018-03-06 | A kind of silt particle separating and dehydrating integrated oil silt particle reduction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108439752A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102225834A (en) * | 2011-05-22 | 2011-10-26 | 黑旋风工程机械开发有限公司 | Sludge treatment method and device for urban drainage pipe network |
| CN102491605A (en) * | 2011-11-16 | 2012-06-13 | 河海大学 | Construction method for carrying out high dehydration on dredging slurry by using swirling flow, condensation, and plate-and-frame |
| CN204824405U (en) * | 2015-07-06 | 2015-12-02 | 新疆石油勘察设计研究院（有限公司） | Silt particle separation cyclic utilization device |
| WO2017067161A1 (en) * | 2015-10-20 | 2017-04-27 | 波鹰(厦门)科技有限公司 | Treatment device and method for oil extraction wastewater |
| CN107098555A (en) * | 2017-06-21 | 2017-08-29 | 陕西欧菲德环保科技有限公司 | The processing unit and its processing method of a kind of greasy dirt |
| CN208362155U (en) * | 2018-03-06 | 2019-01-11 | 胜利油田森诺胜利工程有限公司 | A kind of silt particle separating and dehydrating integrated oil silt particle reduction device |
-
2018
- 2018-03-06 CN CN201810181025.4A patent/CN108439752A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102225834A (en) * | 2011-05-22 | 2011-10-26 | 黑旋风工程机械开发有限公司 | Sludge treatment method and device for urban drainage pipe network |
| CN102491605A (en) * | 2011-11-16 | 2012-06-13 | 河海大学 | Construction method for carrying out high dehydration on dredging slurry by using swirling flow, condensation, and plate-and-frame |
| CN204824405U (en) * | 2015-07-06 | 2015-12-02 | 新疆石油勘察设计研究院（有限公司） | Silt particle separation cyclic utilization device |
| WO2017067161A1 (en) * | 2015-10-20 | 2017-04-27 | 波鹰(厦门)科技有限公司 | Treatment device and method for oil extraction wastewater |
| CN107098555A (en) * | 2017-06-21 | 2017-08-29 | 陕西欧菲德环保科技有限公司 | The processing unit and its processing method of a kind of greasy dirt |
| CN208362155U (en) * | 2018-03-06 | 2019-01-11 | 胜利油田森诺胜利工程有限公司 | A kind of silt particle separating and dehydrating integrated oil silt particle reduction device |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20191213 Address after: 257000 No. 819, North Road, Dongying District, Shandong, Dongying Applicant after: Shandong Yu Yu energy-saving environmental protection technology Co., Ltd. Address before: 257000 Shandong Province, Dongying city the Yellow River Road No. 721 senuo Victory Mansion Applicant before: Shengli Oilfield Sino Shengli Engineering Co., Ltd. |
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| TA01 | Transfer of patent application right |