CN105921486A - Movable oil field waste relative centralization treatment system and treatment method thereof - Google Patents
Movable oil field waste relative centralization treatment system and treatment method thereof Download PDFInfo
- Publication number
- CN105921486A CN105921486A CN201610313370.XA CN201610313370A CN105921486A CN 105921486 A CN105921486 A CN 105921486A CN 201610313370 A CN201610313370 A CN 201610313370A CN 105921486 A CN105921486 A CN 105921486A
- Authority
- CN
- China
- Prior art keywords
- equipment
- oil field
- tank
- field waste
- treatment
- 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
- 238000000034 method Methods 0.000 title claims abstract description 30
- 239000002699 waste material Substances 0.000 title claims abstract description 30
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 17
- 230000003647 oxidation Effects 0.000 claims abstract description 16
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 14
- 239000003814 drug Substances 0.000 claims abstract description 8
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 8
- 229940079593 drug Drugs 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 238000005243 fluidization Methods 0.000 claims description 10
- 238000003672 processing method Methods 0.000 claims description 8
- 238000001704 evaporation Methods 0.000 claims description 6
- 230000008020 evaporation Effects 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 6
- 238000000746 purification Methods 0.000 claims description 6
- 238000003860 storage Methods 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 239000007791 liquid phase Substances 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 239000007790 solid phase Substances 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 3
- 238000005119 centrifugation Methods 0.000 claims description 3
- 239000012141 concentrate Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000000151 deposition Methods 0.000 claims 1
- 238000006213 oxygenation reaction Methods 0.000 claims 1
- 238000005553 drilling Methods 0.000 abstract description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000005188 flotation Methods 0.000 abstract 2
- 238000011272 standard treatment Methods 0.000 abstract 1
- 241001074085 Scophthalmus aquosus Species 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000001052 transient effect Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention provides a movable oil field waste relative centralization treatment system and a treatment method thereof. The movable oil field waste relative centralization treatment system comprises a concoction tank, wherein the concoction tank is connected with a horizontal screw decanter centrifuge through a pipeline; the horizontal screw decanter centrifuge is connected with micro-nano air flotation equipment; the micro-nano air flotation equipment is connected with oxidation equipment; the oxidation equipment is connected with ultrafiltration reverse osmosis equipment; the concoction tank is connected with drug medicine dissolving tank. According to the invention, after standard treatment units of movable treatment equipment are integrated with movable assorted treatment equipment, a set of equipment is designed to be matched with the productivity of a plurality of sets of equipment according to the total amount of well-drilling waste in a block, and a relative centralization type movable treatment station is established, so that the movable oil field waste relative centralization treatment system can meet the environment protection requirements of well-drilling production, can realize low-cost waste treatment, and can be applicable to the requirements of a modern well-drilling waste treatment market.
Description
Technical field
The present invention relates to oil correlative technology field, be specifically related to oil field waste packaged type
Relatively concentrated treatment system and processing method thereof.
Background technology
In this area, the problem being primarily present is that the station construction period is long, processes garbage inadequate
Thoroughly, it is impossible to migrate with the variation of drilling well block, cause garbage haul distance to elongate, increase transport
Cost, extends processing time period, it is impossible to meets drilling well and produces the requirement of moving.
The defect that individual well processes with brill: treating capacity is concentrated not, can not be abundant with boring processing equipment
Play usefulness, cause processing garbage folk prescription high cost, bring pressure to drilling well production cost.
Summary of the invention
For the deficiencies in the prior art, it is an object of the invention to provide a kind of rational in infrastructure,
Oil field waste packaged type relatively concentrated treatment system easy to use and processing method thereof, it
Solve these above-mentioned problems.
The technical solution adopted in the present invention is as follows: at oil field waste packaged type Relatively centralized
Reason system, including modulation tank, described modulation tank connects horizontal screw centrifuge by pipeline, described sleeping
Screw centrifuge connects micro-nano airfloat equipment, and described micro-nano airfloat equipment connects oxidation furnaces,
Described oxidation furnaces connects ultra filtering reverse osmosis equipment, and described modulation tank connects drug dissolving tank.
Preferably, described modulation tank, horizontal screw centrifuge, micro-nano airfloat equipment, oxidation furnaces,
Ultra filtering reverse osmosis equipment and drug dissolving tank are removable dismantled and assembled structure.
Preferably, described horizontal screw centrifuge connects mixer.
Preferably, described pipeline is provided with pipe-line mixer.
Preferably, described modulation tank side is provided with power station.
Oil field waste packaged type Relatively centralized processing method, comprises the steps: garbage
Collecting, fluidisation and homogenizing, centrifugal solid-liquid separates, and super air supporting adds oxidation, and ultrafiltration adds reverse osmosis,
Chemical cleaning method is used to process garbage.
Preferably, after garbage is transported to Relatively centralized treating stations, temporary transient classified storage after reception,
Through mixing fluidisation through centrifugation, solid phase enters biological treatment flow process, and liquid phase enters profit
Separating, micro-nano air supporting high efficiency separation profit, oil enters storage tank, and water enters ozone high grade oxidation
Program laggard enter ultrafiltration reverse osmosis equipment, water purification enter circulating and recovering program, dense water is through super
Reverse osmosis concentrates further, and a small amount of concentrated solution enters evaporation tank natural evaporation, and water purification enters circulation
Water circulation program.
Preferably, if oily waste when mixing fluidisation, then heating is needed.
Preferably, its disposal ability 10 side/hour, process mud: 4-5 side/hour.
The beneficial effect comprise that
The complete place of present invention packaged type processing equipment standard processing unit integrated moveable formula
After reason equipment, design 1 complete equipment and many complete equipments according to the total amount of drilling wastes in block
Production capacity supporting, set up Relatively centralized formula and may move treating stations, disclosure satisfy that drilling well produces simultaneously
Environmental requirement can realize again the cost degradation of offal treatment, it is possible to adapt to current brill and give up
Process market demands.
Accompanying drawing explanation
Fig. 1 is the overall knot of oil field waste packaged type relatively concentrated treatment system of the present invention
Structure schematic diagram.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the present invention is described in detail.
Oil field waste packaged type relatively concentrated treatment system, as it is shown in figure 1, include modulation
Tank 1, described modulation tank 1 connects horizontal screw centrifuge 3, described horizontal screw centrifuge by pipeline 2
3 connect micro-nano airfloat equipment 4, and described micro-nano airfloat equipment 4 connects oxidation furnaces 5,
Described oxidation furnaces 5 connects ultra filtering reverse osmosis equipment 6, and described modulation tank 1 connects drug dissolving tank 7.
Preferably, described modulation tank 1, horizontal screw centrifuge 3, micro-nano airfloat equipment 4, oxygen
Change equipment 5, ultra filtering reverse osmosis equipment 6 and drug dissolving tank 7 are removable dismantled and assembled structure.
Preferably, described horizontal screw centrifuge 2 connects mixer 8.
Preferably, described pipeline 2 is provided with pipe-line mixer 9.
Preferably, described modulation tank 1 side is provided with power station 10.
Oil field waste packaged type Relatively centralized processing method, comprises the steps: garbage
Collecting, fluidisation and homogenizing, centrifugal solid-liquid separates, and super air supporting adds oxidation, and ultrafiltration adds reverse osmosis,
Chemical cleaning method is used to process garbage.
Preferably, after garbage is transported to Relatively centralized treating stations, temporary transient classified storage after reception,
Through mixing fluidisation through centrifugation, solid phase enters biological treatment flow process, and liquid phase enters profit
Separating, micro-nano air supporting high efficiency separation profit, oil enters storage tank, and water enters ozone high grade oxidation
Program laggard enter ultrafiltration reverse osmosis equipment, water purification enter circulating and recovering program, dense water is through super
Reverse osmosis concentrates further, and a small amount of concentrated solution enters evaporation tank natural evaporation, and water purification enters circulation
Water circulation program.
Preferably, if oily waste when mixing fluidisation, then heating is needed.
Preferably, its disposal ability 10 side/hour, process mud: 4-5 side/hour.
Packaged type complete standard handling equipment disposal ability is designed to unit skid, complete process
Ability: average treatment amount 10 side/hour.
Technological principle: waste gathering, fluidisation and homogenizing, centrifugal solid-liquid separates, super air supporting
Adding oxidation, ultrafiltration adds reverse osmosis, and main employing chemical cleaning method processes garbage.This one-tenth is sheathed
After standby process, the liquid phase after offal treatment can reach GB first discharge standard, and solid phase is docked
Native soil second standard can be gone back after later stage biological treatment.
Above-mentioned embodiment is the preferred embodiments of the present invention, is not for limiting the present invention
Enforcement and interest field, all do according to the content described in the present patent application scope of patent protection
The equivalence change gone out and modification, all should be included in scope of the present invention patent.
Claims (9)
1. oil field waste packaged type relatively concentrated treatment system, it is characterised in that include
Modulation tank, described modulation tank connects horizontal screw centrifuge by pipeline, and described horizontal screw centrifuge connects
Micro-nano airfloat equipment, described micro-nano airfloat equipment connects oxidation furnaces, described oxidation furnaces
Connecting ultra filtering reverse osmosis equipment, described modulation tank connects drug dissolving tank.
Oil field waste packaged type Relatively centralized the most according to claim 1 processes system
System, it is characterised in that described modulation tank, horizontal screw centrifuge, micro-nano airfloat equipment, oxidation
Equipment, ultra filtering reverse osmosis equipment and drug dissolving tank are removable dismantled and assembled structure.
Oil field waste packaged type Relatively centralized the most according to claim 1 processes system
System, it is characterised in that described horizontal screw centrifuge connects mixer.
Oil field waste packaged type Relatively centralized the most according to claim 1 processes system
System, it is characterised in that be provided with pipe-line mixer on described pipeline.
Oil field waste packaged type Relatively centralized the most according to claim 1 processes system
System, it is characterised in that described modulation tank side is provided with power station.
6. oil field waste packaged type Relatively centralized processing method, it is characterised in that include
Following steps: waste gathering, fluidisation and homogenizing, centrifugal solid-liquid separates, super air supporting oxygenation
Changing, ultrafiltration adds reverse osmosis, uses chemical cleaning method to process garbage.
Oil field waste packaged type Relatively centralized process side the most according to claim 6
Method, it is characterised in that after garbage is transported to Relatively centralized treating stations, storage of temporarily classifying after reception
Depositing, through mixing fluidisation through centrifugation, solid phase enters biological treatment flow process, and liquid phase enters
Oil-water separation, micro-nano air supporting high efficiency separation profit, oil enters storage tank, and it is senior that water enters ozone
Oxidation procedure laggard enter ultrafiltration reverse osmosis equipment, water purification enter circulating and recovering program, dense water pass through
Super reverse osmosis concentrates further, and a small amount of concentrated solution enters evaporation tank natural evaporation, and water purification enters
Recirculated water reuse program.
Oil field waste packaged type Relatively centralized the most according to claim 6 processes system
System and processing method thereof, it is characterised in that if oily waste when mixing fluidisation, then
Need heating.
Oil field waste packaged type Relatively centralized the most according to claim 6 processes system
System and processing method thereof, it is characterised in that its disposal ability 10 side/hour, process mud:
4-5 side/hour.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610313370.XA CN105921486A (en) | 2016-05-12 | 2016-05-12 | Movable oil field waste relative centralization treatment system and treatment method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610313370.XA CN105921486A (en) | 2016-05-12 | 2016-05-12 | Movable oil field waste relative centralization treatment system and treatment method thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105921486A true CN105921486A (en) | 2016-09-07 |
Family
ID=56835656
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610313370.XA Pending CN105921486A (en) | 2016-05-12 | 2016-05-12 | Movable oil field waste relative centralization treatment system and treatment method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105921486A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113044903A (en) * | 2021-06-01 | 2021-06-29 | 潍坊久宝智能科技有限公司 | Oil-water separator |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002205026A (en) * | 2001-01-04 | 2002-07-23 | Kyowa Eng Kk | Method for treating leftover food |
| CN101690937A (en) * | 2008-04-30 | 2010-04-07 | 濮阳市天地人环保工程技术有限公司 | Process technology for treating drilling waste while drilling before falling onto ground in oil-gas fields |
| CN102452760A (en) * | 2010-10-19 | 2012-05-16 | 中国石油化工股份有限公司 | Treatment method for recycle of oil field produced water |
| CN102849880A (en) * | 2012-09-24 | 2013-01-02 | 杰瑞能源服务有限公司 | Method for comprehensive treatment of oilfield waste |
| CN103013557A (en) * | 2012-12-27 | 2013-04-03 | 北京惠博普能源技术有限责任公司 | Aged effluent oil treatment technology used for oil fields and oil refineries |
| CN204625400U (en) * | 2015-04-02 | 2015-09-09 | 昆山捷斯安环保科技有限公司 | A kind of wastewater treatment suite of equipment |
| CN105084615A (en) * | 2015-09-16 | 2015-11-25 | 成都美富特膜科技有限公司 | Oilfield wastewater treatment process based on special membrane |
| CN205762900U (en) * | 2016-05-12 | 2016-12-07 | 北京华创天宇能源科技有限公司 | Oil field waste packaged type relatively concentrated treatment system |
-
2016
- 2016-05-12 CN CN201610313370.XA patent/CN105921486A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002205026A (en) * | 2001-01-04 | 2002-07-23 | Kyowa Eng Kk | Method for treating leftover food |
| CN101690937A (en) * | 2008-04-30 | 2010-04-07 | 濮阳市天地人环保工程技术有限公司 | Process technology for treating drilling waste while drilling before falling onto ground in oil-gas fields |
| CN102452760A (en) * | 2010-10-19 | 2012-05-16 | 中国石油化工股份有限公司 | Treatment method for recycle of oil field produced water |
| CN102849880A (en) * | 2012-09-24 | 2013-01-02 | 杰瑞能源服务有限公司 | Method for comprehensive treatment of oilfield waste |
| CN103013557A (en) * | 2012-12-27 | 2013-04-03 | 北京惠博普能源技术有限责任公司 | Aged effluent oil treatment technology used for oil fields and oil refineries |
| CN204625400U (en) * | 2015-04-02 | 2015-09-09 | 昆山捷斯安环保科技有限公司 | A kind of wastewater treatment suite of equipment |
| CN105084615A (en) * | 2015-09-16 | 2015-11-25 | 成都美富特膜科技有限公司 | Oilfield wastewater treatment process based on special membrane |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113044903A (en) * | 2021-06-01 | 2021-06-29 | 潍坊久宝智能科技有限公司 | Oil-water separator |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into 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: 20160907 |