CN113137195A - Recycling method and system for base liquid thrown out by oil-based drilling cuttings - Google Patents
Recycling method and system for base liquid thrown out by oil-based drilling cuttings Download PDFInfo
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- CN113137195A CN113137195A CN202110376382.8A CN202110376382A CN113137195A CN 113137195 A CN113137195 A CN 113137195A CN 202110376382 A CN202110376382 A CN 202110376382A CN 113137195 A CN113137195 A CN 113137195A
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- 238000005520 cutting process Methods 0.000 title claims abstract description 62
- 238000004064 recycling Methods 0.000 title claims abstract description 51
- 238000005553 drilling Methods 0.000 title claims abstract description 50
- 238000000034 method Methods 0.000 title claims abstract description 37
- 238000001914 filtration Methods 0.000 claims abstract description 68
- 239000002245 particle Substances 0.000 claims abstract description 47
- 238000005496 tempering Methods 0.000 claims abstract description 44
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- 230000000171 quenching effect Effects 0.000 claims abstract description 8
- 230000009467 reduction Effects 0.000 claims abstract description 6
- 239000012530 fluid Substances 0.000 claims description 42
- 238000000746 purification Methods 0.000 claims description 20
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B21/00—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
- E21B21/06—Arrangements for treating drilling fluids outside the borehole
- E21B21/063—Arrangements for treating drilling fluids outside the borehole by separating components
- E21B21/065—Separating solids from drilling fluids
- E21B21/066—Separating solids from drilling fluids with further treatment of the solids, e.g. for disposal
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/04—Filters with filtering elements which move during the filtering operation with filtering bands or the like supported on cylinders which are impervious for filtering
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/02—Combinations of filters of different kinds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F35/93—Heating or cooling systems arranged inside the receptacle
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/02—Well-drilling compositions
- C09K8/32—Non-aqueous well-drilling compositions, e.g. oil-based
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B21/00—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
- E21B21/01—Arrangements for handling drilling fluids or cuttings outside the borehole, e.g. mud boxes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F2035/99—Heating
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Abstract
The invention relates to a recycling method of base liquid thrown out by oil-based drill cuttings, which comprises the following steps: s1, oil-based drilling cuttings containing base fluidPerforming spin-drying treatment to obtain dry oil-based drilling cuttings and a throwing-off base liquid; s2, quenching and tempering and viscosity reduction treatment are carried out on the thrown base liquid to obtain the thrown base liquid after viscosity is reduced; s3, throwing the base liquid after reducing the viscosity to carry out paper tape filtration to obtain a purified base liquid for removing solid particles, wherein the purified base liquid meets the following requirements: density less than 1.0-1.2g/cm3(ii) a And S4, collecting and storing the purified base liquid for recycling. The invention also relates to a recycling system for the base liquid thrown out by the oil-based drilling cuttings, which comprises a spin dryer, a collecting and tempering device, a paper tape type filter and a collecting tank which are connected in sequence. The method can greatly improve the removal rate of solid particles by quenching and tempering viscosity reduction treatment and paper belt filtration, so that the content and density of solid matters in the purified base liquid reach the recycling standard, and the method has the advantages of low operation cost, simple operation and environmental protection.
Description
Technical Field
The invention belongs to the technical field of drilling waste treatment in the petroleum and natural gas industry, and particularly relates to a recycling method and a recycling system for base liquid thrown out of oil-based drilling cuttings.
Background
The oil-based drilling fluid is a drilling fluid system prepared by adding a matched treating agent by taking oil as a continuous phase, and the oil-based drilling fluid system is obviously superior to a water-based drilling fluid in the aspects of anti-erosion capacity, well wall stabilization, lubricity, reservoir protection and the like, so that the oil-based drilling fluid is widely applied to drilling operations of high-temperature and high-pressure deep wells, large-inclination directional wells, horizontal wells and various complex strata. With the increasing amount of oil-based mud that is returned from drilling, drilling operations generate a large amount of oil-based drill cuttings per day, and each well generates 400-; the oil content of the oil-based drilling cuttings is about 15-30%; meanwhile, the compound contains various toxic and harmful components such as phenolic compounds, heavy metals and the like, and is HW08 type hazardous waste specified in the national hazardous waste records. Thus, effective management and disposal of oil-based drill cuttings has the dual benefits of environmental protection and resource conservation.
Generally, at a drilling operation site, oil-based mud returned from a wellhead is separated into solid-phase oil-based drill cuttings (wet) and liquid-phase base fluid by a solid-liquid separation apparatus such as a shaker, a sand separator, a centrifuge, or the like. The liquid phase base fluid produced in the method is returned to a wellhead by a drilling crew for recycling, which is called as primary recycling, and the solid phase oil-based drilling cuttings (wet) generally contain 20-30% of base oil, so that further solid-liquid separation (drying) through a centrifugal drier is needed.
The oil-based drilling cuttings (wet) are separated into oil-based drilling cuttings (dry) and liquid phase throwing liquid by a centrifugal drier, wherein the oil-based drilling cuttings (dry) account for about 60-70%, and the liquid phase throwing liquid accounts for about 30-40%. The oil content of oil-based drilling cuttings (dry) is generally less than 10 percent, the oil-based drilling cuttings can be directly transported to a professional company for treatment, and the density of liquid phase throwing liquid is about 2.5-3.0g/cm due to the fact that the solid content is too high3The fluidity is poor, the oil can not be directly returned to a wellhead for recycling, and the oil needs to be purified, otherwise, the oil can be transported to a professional company for treatment.
70-95% of the throwing liquid is useful components, and the treatment of the throwing liquid as hazardous waste is a waste of resources, so that an advanced and practical technology and equipment are needed to fully filter solid particles contained in the throwing liquid and ensure that the solid particles meet the technical index requirement of recycling (the density is less than 1.0-1.2 g/cm)3) And secondary recycling of the liquid-phase base liquid is realized.
The existing treatment method of liquid-phase base liquid thrown out by oil-based drilling cuttings is mainly to use a centrifuge method to carry out solid-liquid separation, and the existing main problems are that:
1. the solid content of the liquid phase thrown out of the liquid is high (50-70 percent), the viscosity is high, the particle size of the contained solid is extremely small, the actual removal efficiency of a centrifugal machine on the small particles is not high, and the density after treatment is usually about 1.6-2.0g/cm3And, the recycling requirement cannot be met;
2. the high-speed centrifuge has a high-speed rotating part, so that the failure rate is high, and the energy consumption is high;
3. the operation and use are complex, and the field operation amount is large;
because the centrifuge can not guarantee the performance of the liquid phase (secondary base liquid) to meet the recycling requirement by solid-liquid separation, the liquid phase is thrown out and is directly boxed and transported outside to be treated in most occasions, the generation amount of hazardous wastes is increased, and the recyclable resources are wasted.
Therefore, a method and a system for recycling the base fluid thrown out of the oil-based drill cuttings are needed to solve the above technical problems.
Disclosure of Invention
The invention provides a recycling method for base liquid thrown out by oil-based drilling cuttings, which solves the technical problem.
The technical scheme of the method is as follows:
a recycling method of base liquid thrown out by oil-based drill cuttings comprises the following steps:
s1, carrying out spin-drying treatment on the oil-based drilling cuttings containing the base fluid to obtain dry oil-based drilling cuttings and a thrown-out base fluid;
s2, quenching and tempering and viscosity reduction treatment are carried out on the thrown base liquid to obtain the thrown base liquid after viscosity is reduced;
specifically, the modifying and viscosity reducing treatment is to heat the thrown-out base liquid in step S1, and/or to add a diluent to the thrown-out base liquid in step S1 and then stir the mixture.
The viscosity of the base liquid thrown out is adjusted by heating and/or adding a diluent, the operation is convenient, the process is simple, and the improvement of the working efficiency of the whole process is facilitated.
Further, the diluent is selected from diesel oil or white oil.
S3, throwing the base liquid after reducing the viscosity to carry out paper tape filtration, removing solid particles with large particle size, and obtaining purified base liquid, wherein the purified base liquid meets the following requirements: density less than 1.0-1.2g/cm3;
Specifically, the filtering precision of the paper tape filtering is 15-30 μm.
The solid particles with the particle size of more than 15 mu m can be effectively removed by using paper tape filtration, and the quality of the purified base liquid (the density is less than 1.0-1.2 g/cm) can be ensured in most cases3)。
And S4, collecting and storing the purified base liquid for recycling.
Optionally, the method for recycling the base fluid thrown out by the oil-based drill cuttings comprises the following steps:
s1, carrying out spin-drying treatment on the oil-based drilling cuttings containing the base fluid to obtain dry oil-based drilling cuttings and a thrown-out base fluid;
s2, quenching and tempering and viscosity reduction treatment are carried out on the thrown base liquid to obtain the thrown base liquid after viscosity is reduced;
specifically, the modifying and viscosity reducing treatment is to heat the thrown-out base liquid in step S1, and/or to add a diluent to the thrown-out base liquid in step S1 and then stir the mixture.
The viscosity of the base liquid thrown out is adjusted by heating and/or adding a diluent, the operation is convenient, the process is simple, and the improvement of the working efficiency of the whole process is facilitated.
Further, the diluent is selected from diesel oil or white oil.
S3, the base liquid thrown out after the viscosity is reduced is subjected to paper tape filtration, solid particles with large particle sizes are removed, and a first purification base liquid is obtained and meets the following requirements: the density is 1.0-1.2g/cm3;
Specifically, the filtering precision of the paper tape filtering is 15-30 μm.
The solid particles with the particle size of more than 15 mu m can be effectively removed by using paper tape filtration, and the quality of the purified base liquid (the density is less than 1.0-1.2 g/cm) can be ensured in most cases3) (ii) a In a few cases, when the particle size of the solid particles in the base solution is less than 15 μm, the first purified base solution may not meet the recycling requirement (density is greater than 1.2 g/cm)3)。
S4, the first purification base liquid with the quality which cannot meet the requirements is subjected to filter element filtration, solid particles with small particle sizes are further removed, and second purification base liquid is obtained and meets the following requirements: the density is 1.0-1.2g/cm3。
Specifically, the filtering precision of the filter element is 5-15 μm.
The filter element can effectively remove solid particles with the particle size smaller than 15 mu m by filtration, and is beneficial to reducing the content and the density of the solid particles in the purified base liquid, so that the purified base liquid reaches the recycling standard.
And S5, collecting and storing the second purification base liquid for recycling.
The method has the beneficial effects that:
(1) the removal rate of solid particles (particularly solid particles with small size) is greatly improved, so that the content and density of solid matters in the purified base liquid reach the recycling standard;
(2) the amount of the oil-based drilling cuttings discharged as hazardous waste is reduced by 20-30%, and simultaneously, 20-30% of base liquid in the oil-based drilling cuttings (wet) is recycled;
(3) the operation cost is obviously reduced;
(4) because the high-speed running components such as a centrifugal machine and the like are not used, the energy consumption is reduced, and the failure rate of the device is lower;
(5) the operation is simpler, and the operation intensity of field operation personnel is reduced.
In addition, the invention also provides a treatment system based on the oil-based drilling cutting throwing-out base liquid recycling method, and the specific technical scheme is as follows:
a cyclic utilization system for base liquid thrown out by oil-based drilling cuttings comprises a drying machine, a collecting and tempering device, a paper tape type filter and a collecting tank which are connected in sequence.
Optionally, the oil base drill chip throws away cyclic utilization system of base liquid, including drier, collection quenching and tempering device, paper tape filter, filter core filter and the holding vessel who connects in order.
Specifically, the collecting and tempering device comprises two tempering tank bodies with the same structure, wherein the two tempering tank bodies are connected in parallel and are alternately used, namely one tank is used for collecting and one tank is used for tempering;
a heater and a stirrer are arranged in each tempering tank body;
every first inlet, first liquid outlet and first notes liquid mouth have been seted up to the quenching and tempering jar body.
Specifically, the paper tape filter includes: a liquid storage tank, a filter paper tape, a paper tape conveying mechanism, an outlet pump and a waste storage box,
the liquid storage tank is internally provided with a filter paper tape which divides the liquid storage tank into a second liquid inlet cavity and a second liquid outlet cavity.
The filtering paper tape is a continuous non-woven fabric tape made of polypropylene fibers or polyester fibers.
The filtering precision of the filtering paper tape is 15-30 mu m. The device can effectively remove solid particles with the particle size larger than 15 mu m;
the paper tape conveying mechanism is a flat screen type paper tape conveying mechanism or a drum type paper tape conveying mechanism, and the paper tape conveying mechanism is arranged on the liquid storage tank.
Further, the paper tape conveying mechanism comprises a paper tape winding frame, a supporting mesh tape and a driving motor, wherein the supporting mesh tape is arranged in the liquid storage tank, is positioned below the filtering paper tape and is used for supporting the filtering paper tape; under the action of the driving motor, the supporting net drives the filtering paper tape to penetrate through the liquid storage tank, so that the filtering paper tape is automatically replaced.
When the paper tape is blocked by the trapped pollutants, resulting in a reduction in filtration capacity, the paper tape transport mechanism automatically operates, is replaced with a new filter paper tape, and simultaneously delivers the used filter paper tape (contaminated) to the waste storage bin.
The waste storage box is used for filtering paper tapes after being used so as to be delivered to a professional company for treatment;
the head of the outlet pump provides vacuum degree required by paper tape filtration and conveying pressure required by subsequent process equipment. Thus, the outlet pump can meet the conveying requirement of the whole system, is used for pumping the filtered base liquid and provides the required lift (pressure) of the subsequent filtering equipment.
The outlet pump is connected with the bottom of the liquid outlet cavity through a pipeline.
The filtering principle of the paper tape type filter is as follows: get rid of on base fluid distributes the filter paper area after getting into the feed liquor chamber, hold back down the pollutant, along with the increase of the pollutant of holding back, the resistance of filtering the paper tape is also increasing, and when the resistance reached a definite value, the liquid level rose until the critical value, drags the automatic change of filtering the paper tape, and the filtration paper tape that has used gets into in the waste storage box to realize not shutting down the operation.
Specifically, a paper folding filter element is arranged in the filter element filter; the filtering precision of the filter element filter is 5-15 mu m;
further, the filter element filter is a vertical filter element filter; the filter element filter comprises a third shell and a third filter element group, the third filter element group is arranged in the third shell, and the third shell is provided with a third liquid inlet, a third liquid outlet and a third sewage outlet.
Optionally, the filter element filter is a vertical filter element filter or a horizontal filter element filter.
It is understood that by vertical cartridge filter is meant that the housing of the cartridge filter is vertical; the horizontal filter element filter means that a shell of the filter element filter is horizontal.
The system of the invention has the advantages that:
(1) the removal rate of solid particles (particularly solid particles with small size) is greatly improved, so that the content and density of solid matters in the purified base liquid reach the recycling standard;
(2) the amount of the oil-based drilling cuttings discharged as hazardous waste is reduced by 20-30%, and simultaneously, 20-30% of base liquid in the oil-based drilling cuttings (wet) is recycled;
(3) the operation cost is obviously reduced;
(4) because the high-speed running components such as a centrifugal machine and the like are not used, the energy consumption is reduced, and the failure rate of the device is lower;
(5) the operation is simpler, and the operation intensity of field operators is reduced;
(6) the system of the invention has low cost which is 40 percent lower than that of a centrifuge.
Drawings
FIG. 1 is a schematic flow chart of the recycling method of the present invention;
FIG. 2 is a schematic structural diagram of the recycling system of the present invention;
FIG. 3 is a schematic structural view of a collecting and conditioning device according to the present invention;
FIG. 4 is a first schematic view of the structure of the paper belt filter of the present invention;
FIG. 5 is a second schematic structural view of the paper belt filter of the present invention;
FIG. 6 is a schematic view of the combination of the level sensor, PLC controller and tape filter mechanism of the present invention;
FIG. 7 is a first schematic view of a cartridge filter according to the present invention;
fig. 8 is a schematic structural diagram of a filter element filter of the invention.
In the drawings, the components represented by the respective reference numerals are listed below:
1. a spin dryer;
2. collecting a tempering device; 21. tempering the tank body; 22. a first liquid inlet; 23. a first liquid outlet; 24. a first liquid injection port; 25. a heater; 26. a stirrer;
3. a paper tape type filter; 31. a liquid storage tank; 311. a second liquid inlet; 312. a second liquid outlet; 313. a second paper feed port; 314. a second paper outlet; 315. a second liquid inlet cavity; 316. a second liquid outlet cavity; 32. filtering the paper tape; 33. a paper tape transport mechanism; 331. a paper tape roll stand; 332. supporting the mesh belt; 333. a drive motor; 334. a guide member; 34. an outlet pump; 35. a waste collection bin;
4. a cartridge filter; 41. a third housing; 42. a third filter element group; 43. a third liquid inlet; 44. a third liquid outlet; 45. a third sewage draining outlet;
5. a collection tank;
400. a liquid level sensor;
500. a PLC controller.
Detailed Description
The principles and features of this invention are described below in conjunction with the following drawings, which are set forth by way of illustration only and are not intended to limit the scope of the invention.
In the description of the present invention, it is to be understood that the terms "central," "longitudinal," "lateral," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," and the like are used in the orientation or positional relationship indicated in the drawings, which are merely for convenience in describing the invention and to simplify the description, and are not intended to indicate or imply that the referenced device or element must have a particular orientation, be constructed and operated in a particular orientation, and are therefore not to be construed as limiting the invention. Furthermore, the terms "first", "second", etc. are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first," "second," etc. may explicitly or implicitly include one or more of that feature. In the description of the invention, the meaning of "a plurality" is two or more unless otherwise specified.
In the description of the invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted", "connected" and "connected" are to be construed broadly, e.g. as being fixed or detachable or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the creation of the present invention can be understood by those of ordinary skill in the art through specific situations.
The following is a preferred description of the invention with reference to figures 1-8:
example 1
The embodiment provides a recycling method for base liquid thrown out by oil-based drill cuttings, which comprises the following steps:
s1, carrying out spin-drying treatment on the oil-based drilling cuttings containing the base fluid to obtain dry oil-based drilling cuttings and a thrown-out base fluid;
s2, heating the thrown base liquid at 38 ℃ to obtain the thrown base liquid after viscosity is reduced, wherein the thrown base liquid after viscosity is reduced meets the following requirements: viscosity of 149 pas;
s3, throwing the base liquid after reducing the viscosity to carry out paper tape filtration, wherein the base liquid is obtained by filteringThe filtering precision of the paper tape filtering is 15 microns, solid particles with the particle size of 15 microns are removed, and a purification base solution is obtained, wherein the purification base solution meets the following requirements: the density was 1.1g/cm3;
And S4, collecting and storing the purified base liquid for recycling.
In the present embodiment, the above-mentioned method for recycling base liquid thrown off based on oil-based drill cuttings is implemented by a system for recycling base liquid thrown off based on oil-based drill cuttings as shown in fig. 1 to 4, the system comprises a spin dryer 1, a collecting and tempering device 2, a paper tape type filter 3 and a collecting tank 5 which are connected in sequence;
as shown in fig. 3, the collecting and tempering device 2 includes two tempering tank bodies 21 with the same structure, and the two tempering tank bodies 21 are installed in parallel and used alternately, that is, one tank is used for collecting and one tank is used for tempering;
a heater 25 and a stirrer 26 are arranged in each tempering tank body 21;
each tempering tank body 21 is provided with a first liquid inlet 22, a first liquid outlet 23 and a first liquid filling port 24.
As shown in fig. 4, the paper belt filter 3 includes: a reservoir 31, a filter paper tape 32, a tape transport mechanism 33, an outlet pump 34 and a waste storage tank 35, wherein,
the upper part of the liquid storage tank 31 is provided with a second liquid inlet 311, and the lower part of the liquid storage tank 31 is provided with a second liquid outlet 312; a second paper inlet 313 is formed in the upper part of the liquid storage tank 31, and a second paper outlet 314 is formed in the side surface of the liquid storage tank 31;
the paper tape conveying mechanism 33 is a flat-screen type paper tape conveying mechanism, the paper tape conveying mechanism 33 comprises a paper tape roll frame 331, a flat-bed type supporting mesh belt 332, a driving motor 333 and a cylindrical guide component 334, and the flat-bed type supporting mesh belt 332 is arranged in the liquid storage tank 31, is positioned below the filter paper tape 32 and is used for supporting the filter paper tape 32; under the action of the driving motor 333, the supporting mesh belt 332 drives the filtering paper belt 32 to pass through the liquid storage tank 31 and be sent out from the second paper feeding port 313, so that the filtering paper belt 32 is automatically replaced; the cylindrical guide member 334 is disposed in the liquid storage tank 31 and above the filter paper tape 32, and is used for pressing the filter paper tape 32;
the filter paper tape 32 is arranged in the liquid storage tank 31, and the liquid storage tank 31 is divided into a second liquid inlet cavity 315 communicated with the second liquid inlet 311 and a second liquid outlet cavity 316 communicated with the second liquid outlet 312 by the filter paper tape 32; the filter paper tape 32 is a continuous non-woven fabric tape made of polyester fiber; the filtering precision of the filtering paper tape 32 is 15 mu m;
the paper tape conveying mechanism 33 is mounted on the liquid storage tank 31 and is used for supporting the filter paper tape 32 and driving the filter paper tape 32 to pass through the liquid storage tank 31, and the waste storage box 35 is arranged below the second paper outlet 314 and is used for collecting the used filter paper tape 32;
the outlet pump 34 is connected with the second liquid outlet 312 through a pipeline, and the head of the outlet pump 34 provides the vacuum degree required by the paper tape filtration and the conveying pressure required by the subsequent process equipment;
after being treated by the paper tape type filter 3, the solid particles in the inlet water are effectively removed, and the water quality index of the purified base liquid reaches: the density was 1.1g/cm3。
The actual operation effect of this embodiment is: the effluent quality index is good, the content and density of solids in the purified base fluid reach the recycling standard, the amount of the oil-based drilling cuttings discharged as hazardous waste is reduced by 22%, and meanwhile 22% of the base fluid in the oil-based drilling cuttings (wet) is recycled; compared with the conventional centrifugal machine, the energy consumption and the material consumption of the centrifugal machine save the equipment cost by 42 percent.
Example 2
The embodiment provides a recycling method for base liquid thrown out by oil-based drill cuttings, which comprises the following steps:
s1, carrying out spin-drying treatment on the oil-based drilling cuttings containing the base fluid to obtain dry oil-based drilling cuttings and a thrown-out base fluid;
s2, adding diesel oil into the thrown-off base liquid, stirring and mixing, wherein the mass ratio of the thrown-off base liquid to the diesel oil is 1:1.2, heating the thrown-off base liquid after stirring and mixing at the heating temperature of 40 ℃ to obtain the thrown-off base liquid after reducing the viscosity, and the thrown-off base liquid after reducing the viscosity meets the following requirements: viscosity of 142 pas;
s3, throwing the base liquid after the viscosity is reduced to carry out paper tape filtration, wherein the filtration precision of the paper tape filtration is 30 microns, and removing solid particles with the particle size of 30 microns to obtain first purification base liquid, wherein the first purification base liquid meets the following requirements: the density was 0.8g/cm3;
S4, the first purification base liquid with the quality which cannot meet the requirements is subjected to filter element filtration, solid particles with small particle sizes are further removed, and second purification base liquid is obtained and meets the following requirements: the density was 0.8g/cm3。
And S5, collecting and storing the second purification base liquid for recycling.
In the present embodiment, the above-mentioned recycling method based on the base fluid thrown off by the oil-based drill cuttings is implemented by a recycling system of the base fluid thrown off by the oil-based drill cuttings as shown in fig. 1, fig. 2, fig. 3, fig. 5 and fig. 7, the system comprises a drying machine 1, a collecting and tempering device 2, a paper tape type filter 3, a filter element filter 4 and a collecting tank 5 which are connected in sequence;
as shown in fig. 3, the collecting and tempering device 2 includes two tempering tank bodies 21 with the same structure, and the two tempering tank bodies 21 are installed in parallel and used alternately, that is, one tank is used for collecting and one tank is used for tempering;
a heater 25 and a stirrer 26 are arranged in each tempering tank body 21;
each tempering tank body 21 is provided with a first liquid inlet 22, a first liquid outlet 23 and a first liquid filling port 24.
As shown in fig. 5, the paper belt filter 3 includes: a reservoir 31, a filter paper tape 32, a tape transport mechanism 33, an outlet pump 34 and a waste storage tank 35, wherein,
the upper part of the liquid storage tank 31 is provided with a second liquid inlet 311, and the lower part of the liquid storage tank 31 is provided with a second liquid outlet 312; a second paper inlet 313 is formed in the upper part of the liquid storage tank 31, and a second paper outlet 314 is formed in the side surface of the liquid storage tank 31;
the paper tape conveying mechanism 33 is a drum-type paper tape conveying mechanism, the paper tape conveying mechanism 33 comprises a paper tape winding frame 331, an arc-shaped supporting mesh belt 332, a driving motor 333 and a cylindrical guide component 334, and the arc-shaped supporting mesh belt 332 is arranged in the liquid storage tank 31, is positioned below the filtering paper tape 32 and is used for supporting the filtering paper tape 32; under the action of the driving motor 333, the supporting mesh belt 332 drives the filtering paper belt 32 to pass through the liquid storage tank 31 and be sent out from the second paper feeding port 313, so that the filtering paper belt 32 is automatically replaced; the cylindrical guide member 334 is disposed in the liquid storage tank 31 and above the filter paper tape 32, and is used for pressing the filter paper tape 32;
the filter paper tape 32 is arranged in the liquid storage tank 31, and the liquid storage tank 31 is divided into a second liquid inlet cavity 315 communicated with the second liquid inlet 311 and a second liquid outlet cavity 316 communicated with the second liquid outlet 312 by the filter paper tape 32; the filter paper tape 32 is a continuous non-woven fabric tape made of polyester fiber; the filtering precision of the filtering paper tape 32 is 30 mu m;
the paper tape conveying mechanism 33 is mounted on the liquid storage tank 31 and is used for supporting the filter paper tape 32 and driving the filter paper tape 32 to pass through the liquid storage tank 31, and the waste storage box 35 is arranged below the second paper outlet 314 and is used for collecting the used filter paper tape 32;
the outlet pump 34 is connected to the second liquid outlet 312 through a pipe, and the head of the outlet pump 34 provides a vacuum degree required for paper tape filtration and a conveying pressure required by subsequent process equipment.
As shown in fig. 7, the cartridge filter 4 is a vertical cartridge filter; the filter element filter 4 comprises a third shell 41 and a third filter element group 42, the third filter element group 42 is arranged in the third shell 41, and the third shell 41 is provided with a third liquid inlet 43, a third liquid outlet 44 and a third sewage outlet 45;
the third filter element group 42 is a paper folding filter element group, and the filtering precision of the paper folding filter element group is 5 μm.
Solid particles in the influent water, particularly solids in the influent water, after treatment in a paper-belt filter 3Fine solid particles are effectively removed, and the water quality index of the second purification base liquid reaches: the density was 0.8g/cm3。
The actual operation effect of this embodiment is: the effluent quality index is good, the content and density of solids in the second purified base fluid reach the recycling standard, the amount of the oil-based drilling cuttings discharged as hazardous waste is reduced by 29%, and 29% of base fluid in the oil-based drilling cuttings (wet) is recycled; compared with the conventional centrifugal machine, the energy consumption and the material consumption of the centrifugal machine save the equipment cost by 48 percent.
Example 3
The embodiment provides a recycling method for base liquid thrown out by oil-based drill cuttings, which comprises the following steps:
s1, carrying out spin-drying treatment on the oil-based drilling cuttings containing the base fluid to obtain dry oil-based drilling cuttings and a thrown-out base fluid;
s2, adding white oil into the thrown-off base liquid, stirring and mixing, wherein the mass ratio of the thrown-off base liquid to the white oil is 1:1, heating the stirred and mixed thrown-off base liquid at the heating temperature of 35 ℃, obtaining the thrown-off base liquid after reducing the viscosity, and meeting the requirement of the thrown-off base liquid after reducing the viscosity: viscosity is lower than 138 pas;
s3, throwing the base liquid after the viscosity is reduced to carry out paper tape filtration, wherein the filtration precision of the paper tape filtration is 20 microns, and removing solid particles with the particle size of 20 microns to obtain first purification base liquid, wherein the first purification base liquid meets the following requirements: the density was 0.9g/cm3;
S4, the first purification base liquid with the quality which cannot meet the requirements is subjected to filter element filtration, solid particles with small particle sizes are further removed, and second purification base liquid is obtained and meets the following requirements: the density was 0.9g/cm3。
And S5, collecting and storing the second purification base liquid for recycling.
In the present embodiment, the above-mentioned recycling method based on the base fluid thrown off by the oil-based drill cuttings is implemented by the recycling system of the base fluid thrown off by the oil-based drill cuttings as shown in fig. 1, fig. 2, fig. 3, fig. 4 and fig. 8, the system comprises a drying machine 1, a collecting and tempering device 2, a paper tape type filter 3, a filter element filter 4 and a collecting tank 5 which are connected in sequence;
as shown in fig. 3, the collecting and tempering device 2 includes two tempering tank bodies 21 with the same structure, and the two tempering tank bodies 21 are installed in parallel and used alternately, that is, one tank is used for collecting and one tank is used for tempering;
a heater 25 and a stirrer 26 are arranged in each tempering tank body 21;
each tempering tank body 21 is provided with a first liquid inlet 22, a first liquid outlet 23 and a first liquid filling port 24.
As shown in fig. 4, the paper belt filter 3 includes: a reservoir 31, a filter paper tape 32, a tape transport mechanism 33, an outlet pump 34 and a waste storage tank 35, wherein,
the upper part of the liquid storage tank 31 is provided with a second liquid inlet 311, and the lower part of the liquid storage tank 31 is provided with a second liquid outlet 312; a second paper inlet 313 is formed in the upper part of the liquid storage tank 31, and a second paper outlet 314 is formed in the side surface of the liquid storage tank 31;
the paper tape conveying mechanism 33 is a flat-screen type paper tape conveying mechanism, the paper tape conveying mechanism 33 comprises a paper tape roll frame 331, a flat-bed type supporting mesh belt 332, a driving motor 333 and a cylindrical guide component 334, and the flat-bed type supporting mesh belt 332 is arranged in the liquid storage tank 31, is positioned below the filter paper tape 32 and is used for supporting the filter paper tape 32; under the action of the driving motor 333, the supporting mesh belt 332 drives the filtering paper belt 32 to pass through the liquid storage tank 31 and be sent out from the second paper feeding port 313, so that the filtering paper belt 32 is automatically replaced; the cylindrical guide member 334 is disposed in the liquid storage tank 31 and above the filter paper tape 32, and is used for pressing the filter paper tape 32;
the filter paper tape 32 is arranged in the liquid storage tank 31, and the liquid storage tank 31 is divided into a second liquid inlet cavity 315 communicated with the second liquid inlet 311 and a second liquid outlet cavity 316 communicated with the second liquid outlet 312 by the filter paper tape 32; the filter paper tape 32 is a continuous non-woven fabric tape made of polyester fiber; the filtering precision of the filtering paper tape 32 is 20 mu m;
the paper tape conveying mechanism 33 is mounted on the liquid storage tank 31 and is used for supporting the filter paper tape 32 and driving the filter paper tape 32 to pass through the liquid storage tank 31, and the waste storage box 35 is arranged below the second paper outlet 314 and is used for collecting the used filter paper tape 32;
the outlet pump 34 is connected with the second liquid outlet 312 through a pipeline, and the head of the outlet pump 34 provides the vacuum degree required by the paper tape filtration and the conveying pressure required by the subsequent process equipment;
as shown in fig. 8, the cartridge filter 4 is a horizontal cartridge filter 4; the filter element filter 4 comprises a third shell 41 and a third filter element group 42, the third filter element group 42 is arranged in the third shell 41, and the third shell 41 is provided with a third liquid inlet 43, a third liquid outlet 44 and a third sewage outlet 45;
the third filter element group 42 is a paper folding filter element group, and the filtering precision of the paper folding filter element group is 15 μm.
After being treated by the paper tape type filter 3, solid particles, especially fine solid particles in the inlet water are effectively removed, and the water quality index of the second purification base liquid reaches: the density was 0.9g/cm3。
The actual operation effect of this embodiment is: the effluent quality index is good, the content and density of solids in the second purified base fluid reach the recycling standard, the amount of the oil-based drilling cuttings discharged as hazardous waste is reduced by 26%, and meanwhile, 26% of base fluid in the oil-based drilling cuttings (wet) is recycled; compared with the conventional centrifugal machine, the energy consumption and the material consumption of the centrifugal machine save 47 percent of the equipment cost.
Further, in order to realize the automatic replacement of the filtering paper tape 32, the paper tape type filter 3 of the above embodiments 1 to 3 should be provided with a control structure, as shown in fig. 6, the paper tape type filter 3 further includes a PLC controller 500 and a liquid level sensor 400 fixedly disposed in the liquid storage tank 31, the liquid level sensor 400 is connected with an input end of the PLC controller 500 through a wire, and an output end of the PLC controller 500 is connected with the paper tape conveying mechanism 33 through a wire. Further, an output terminal of the PLC controller 500 is connected to the driving motor 333 through a wire.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.
Claims (9)
1. A recycling method for base liquid thrown out by oil-based drill cuttings is characterized by comprising the following steps:
s1, carrying out spin-drying treatment on the oil-based drilling cuttings containing the base fluid to obtain dry oil-based drilling cuttings and a thrown-out base fluid;
s2, quenching and tempering and viscosity reduction treatment are carried out on the thrown base liquid to obtain the thrown base liquid after viscosity is reduced;
s3, throwing the base liquid after reducing the viscosity to carry out paper tape filtration, removing solid particles with large particle size, and obtaining purified base liquid, wherein the purified base liquid meets the following requirements: density less than 1.0-1.2g/cm3;
And S4, collecting and storing the purified base liquid for recycling.
2. The method for recycling the base fluid thrown away by oil-based drill cuttings according to claim 1, wherein in step S2, the modifying and viscosity reducing treatment is to heat the base fluid thrown away in step S1, and/or to add a diluent to the base fluid thrown away in step S1 and stir the mixture.
3. The method of claim 2, wherein the diluent is selected from diesel or white oil.
4. The method for recycling the base fluid thrown off by the oil-based drill cuttings according to claim 1, wherein in the step S3, the filtering precision of the paper tape filtering is 15 μm to 30 μm.
5. The recycling method of the oil-based drill cuttings throwing-off base fluid according to any one of claims 1 to 4, wherein a filter element filtering step S5 is further included between the step S3 and the step S4, specifically, the purification base fluid from which the large-particle-size particles are removed is subjected to filter element filtering, and further solid particles with smaller particle sizes are removed, so that the purification base fluid is obtained.
6. The method for recycling the base fluid thrown away by the oil-based drill cuttings according to claim 5, wherein the filtering precision of the filtering of the filter element is 5-15 μm.
7. The utility model provides a cyclic utilization system of oil base drill chip throw-off base liquid which characterized in that includes drier (1), collection quenching and tempering device (2), paper tape filter (3) and holding vessel (5) that connect in order.
8. The oil-based drill cuttings base fluid recycling system according to claim 7, characterized in that a filter element filter (4) is further disposed between the paper belt filter (3) and the collection tank (5), and the spin dryer (1), the collection conditioning device (2), the paper belt filter (3), the filter element filter (4) and the collection tank (5) are sequentially connected.
9. The recycling system of the base fluid thrown out by the oil-based drill cuttings according to claim 7 or 8, wherein the collecting and tempering device (2) comprises two tempering tank bodies (21) with identical structures, and the two tempering tank bodies (21) are installed in parallel and used alternately, namely one tank collecting and one tank tempering;
a heater (25) and a stirrer (26) are arranged in each tempering tank body (21);
each tempering tank body (21) is provided with a first liquid inlet (22), a first liquid outlet (23) and a first liquid injection port (24).
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