CN104946235A - Preparation method of self-suspension proppant and prepared proppant - Google Patents
Preparation method of self-suspension proppant and prepared proppant Download PDFInfo
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- C09K8/80—Compositions for reinforcing fractures, e.g. compositions of proppants used to keep the fractures open
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Abstract
The invention discloses a preparation method of a self-suspension proppant. The self-suspension proppant is prepared by dispersing a water-soluble polymer material into an aggregate at 15-150 DEG C, wherein the water-soluble polymer material is selected from natural polymer materials, artificially synthesized polymer materials or semi-naturally semi-artificially synthesized polymer materials, and the use amount of the water-soluble polymer material accounts for 0.1-15wt% of that of the aggregate. By virtue of optimized selection of raw materials and process conditions, a preparation process of the proppant which covers the polymer material simply, conveniently and effectively is dramatically obtained, the material cost is reduced, and a used covering material cannot cause pollution to the environment. The self-suspension fracturing proppant disclosed by the invention does not need high-cost fracturing fluid containing organic high polymers to perform fracturing, but directly uses natural water available everywhere to perform fracturing, so that pollution is reduced, and the cost is reduced.
Description
Technical field
The invention belongs to the fluid mineral exploitation fields such as oil, Sweet natural gas and shale gas, be specifically related to a kind of propping agent by support reinforcing crack and preparation method thereof.
Background technology
Support fracturing method adopts fracturing propping agents pressure break and support fracturing, to improve the oil recovery of fracture flow capacity or to adopt the method for Sweet natural gas.
In existing support fracturing technology, mainly comprise and use propping agent and fracturing liquid (active water, linear glue or frozen glue) two portions, fracturing liquid and propping agent are two independently systems, and fracturing liquid flow at high speed, utilizes turbulent suspension propping agent.Conventional propping agent is quartz sand or haydite.But after propping agent arrives crack, due to declining to a great extent of rate of flow of fluid, propping agent rapid subsidence is in Slit bottom.On the other hand, the macromolecular compound used in drag reduction water enters stratum in company with clear water, and the viscosity of drag reduction water increases, and when the row of returning, consumes very large pump horsepower, and is unfavorable for all rows of returning; The macromolecular compound that part stays underground blocks the hole on stratum, cause that oil pump capacity declines, macromolecular compound by layer gap to permeate the ground water, cause water pollution.
Summary of the invention
For the weak point that prior art exists, the object of this invention is to provide a kind of preparation method from suspension fracturing propping agents.
Another object of the present invention is to provide the fracturing propping agents that certainly suspend that described preparation method obtains.
For achieving the above object, concrete technical scheme is:
From a preparation method for suspension fracturing propping agents, be under 15-150 DEG C of condition, water-soluble high-molecular material be scattered in aggregate obtained;
Described water-soluble high-molecular material is the organic materials of meeting water Fast-swelling or dissolving, be selected from the macromolecular material of natural macromolecular material, synthetic macromolecular material or half-natural semi-artificial synthesis, the consumption of described water-soluble high-molecular material is 0.1 ~ 15wt% of aggregate consumption.
Described aggregate is have one or more of the solid particulate that bears crack closure stress sufficient mechanical strength, preferably, described aggregate is one or more in the shell particle of quartz sand, haydite, metallic particles, globular glass particle, sintered bauxite, sintered alumina, sintered zirconia, synthetic resins, precoated sand, pulverizing; Described aggregate is of a size of 6-200 order (namely between 2.8mm-0.075mm).
The metal material that wherein metallic particles preferred hardness is high, such as, the material of described metallic particles is one or more in carbon steel, stainless steel, aluminium alloy, iron-nickel alloy, Ferro Manganese.
Preferably, described natural macromolecular material is selected from vegetable jelly, gelatin or microbiological gum; Described vegetable jelly be gum arabic, tragacanth gum, locust bean gum, guanidine glue, sesbania gum, rubber made from soybean cake, in one or more; Described gelatin is one or more in gelatine, gelatin, casein food grade, chitosan; Described microbiological gum be selected from xanthan gum, gelling gum, (Gellan gum), curdlan (Curdlan) one or more;
The macromolecular material of described synthetic comprises condensation class and polymeric type macromolecular material; Wherein, condensation family macromolecule material is selected from one or more in versamid 900, aminoresin and urethane resin; Polymeric type macromolecular material be selected from polyacrylamide, polyacrylic acid, polyoxyethylene glycol, polyoxyethylene, polymaleic anhydride, polyquaternium one or more;
The macromolecular material of described half-natural semi-artificial synthesis comprises treated starch, modified-cellulose and modified plant gum, is specifically selected from one or more in carboxymethyl starch, Walocel MT 20.000PV, methylcellulose gum, ethyl cellulose, Natvosol, propyloic starch, starch acetates, methylol guar gum, hydroxypropylguar gum, Carboxymethyl hydroxypropyl guar.
Preferably, described preparation method is under 15-60 DEG C of condition, is scattered in by aggregate in water-soluble high-molecular material obtained;
Described water-soluble high-molecular material is selected from the one in vegetable jelly, gelatin or microbiological gum, and the consumption of described water-soluble high-molecular material is the 0.5-15wt% of aggregate consumption.
Further, step that is dry and screening is also comprised.
Or described preparation method is under 80-150 DEG C of condition, aggregate is scattered in water-soluble high-molecular material obtained;
Wherein, described water-soluble high-molecular material be selected from polyacrylamide, polyacrylic acid, polyoxyethylene glycol, polyoxyethylene, polymaleic anhydride, polyquaternium, carboxymethyl starch, Walocel MT 20.000PV, methylcellulose gum, ethyl cellulose, Natvosol, propyloic starch, starch acetates, methylol guar gum, hydroxypropylguar gum, Carboxymethyl hydroxypropyl guar one or more;
The consumption of described water-soluble polymer is the 0.1-15wt% of aggregate consumption.
Further, aggregate is first warming up to 170-200 DEG C by described preparation method, then treats that aggregate is cooled to 80-150 DEG C, is scattered in water-soluble high-molecular material by aggregate.
Preparation method of the present invention prepare from suspended prop.
What the present invention also proposed prepare from the application of suspended prop in the fluid mineral exploitations such as oil, Sweet natural gas and shale gas.
Particularly, described application is mixing the present invention's proposition according to the part by weight 1:3-8 of water from suspended prop, passes in mineral reserve, play the effect of support fracturing after stirring.Described water refers to clear water, is selected from tap water or surface water, underground water.Do not add chemical.
Beneficial effect of the present invention is:
By the optimized choice to raw material and processing condition, obtain the preparation technology of simple and effective coated high molecular materials for support agent breakthroughly, and reduce material cost, the coating material of use can not to environment;
What the present invention proposed with the addition of organic polymer and the fracturing liquid of cost intensive carries out pressure break from suspension fracturing propping agents without the need to using, and directly uses the natural water be available anywhere to carry out pressure break, therefore, reduces pollution, reduces cost.
It is long from suspension fracturing propping agents suspension time in clear water that the present invention proposes, and can better meet the needs of oil recovery.What the present invention proposed can reduce of the fracturing fluid frictional resistance from suspension fracturing propping agents, makes to apply pressure break support system of the present invention and has substantially identical performance with existing fracturing liquid, easily carry, easily the row of returning.
Embodiment
Following examples for illustration of the present invention, but are not used for limiting the scope of the invention.
Embodiment 1
1) with quartz sand (river sand) for raw material, through cleaning, after 120 DEG C of 5h dry, completely not moisture in sand, screening 20-40 object quartz sand 1000g is aggregate;
2) guanidine glue (viscosity at room temperature 150mPa.S) 8g is added under room temperature.Stir.After dry cooling, screening.
The propping agent obtained after screening is particle diameter 20-40 object particle (slightly larger than aggregate size), and aggregate surface is coated or be partly coated with guanidine glue macromolecular material.
Embodiment 2
1) 40-70 order 1kg quartz sand (river sand) is got as aggregate, for subsequent use;
2) xanthan gum 10g(viscosity at room temperature 2000mPa.S is added under room temperature), Homogeneous phase mixing.
3) screening after cooling, to obtain final product.
Embodiment 3
1) 30-50 order 1kg quartz sand (aeolian sand) is got as aggregate, for subsequent use;
2) first quartz sand is heated to 200 DEG C, when aggregate temperature is down to 130 DEG C naturally, by the aqueous solution that carboxy-methyl hydroxy propyl guanidine glue 5g is mixed with 20%, adds aggregate and Homogeneous phase mixing;
3) dry rear, screening, to obtain final product.
Comparative example 1
Propping agent: quartz sand, granularity 20-40 order.
Sedimentation experiment in natural water (not adding chemical).
The settling velocity of embodiment 1-3, comparative example 1 propping agent in table 1 natural water
Embodiment 4
1) 30-50 order 1kg haydite is got as aggregate, for subsequent use;
2) be heated to 200 DEG C, when temperature is down to 140 DEG C, add 50% aqueous solution of 5g anion-polyacrylamide, Homogeneous phase mixing;
3) by above-mentioned steps 2) in mixture drying screening, to obtain final product.
Embodiment 5
1) 40-70 order 1kg haydite is got as aggregate, for subsequent use;
2) be heated to 200 DEG C, when aggregate temperature is down to 140 DEG C naturally, add 50% aqueous solution of 10g carboxymethyl cellulose, Homogeneous phase mixing;
3) mixture in above-mentioned steps (2) is dry, screening, to obtain final product.
Comparative example 2
Propping agent: with 20-40 order haydite for propping agent.
Embodiment 4 in table 2 natural water, 5, the settling velocity of comparative example 2 propping agent
Embodiment 6
1) 30-50 order 1kg precoated sand (the method manufacture according to patent CN1274626A embodiment 1) is got as aggregate, for subsequent use;
2) be heated to 200 DEG C, when temperature is down to 130 DEG C, add 50% aqueous solution of 5g anion-polyacrylamide (molecular weight 3,000,000), Homogeneous phase mixing;
3) by above-mentioned steps 2) in dry, the screening of mixture, to obtain final product.
Embodiment 7
1) 70-140 order 1kg glass microsphere is got as aggregate, for subsequent use;
2) be heated to 200 DEG C, when temperature is down to 140 DEG C naturally, add 30% aqueous solution of 10g carboxy-methyl hydroxy propyl guanidine glue, Homogeneous phase mixing;
3) by above-mentioned steps 2) in dry, the screening of mixture, to obtain final product.
Embodiment 8
1) nut-shell of 40-70 order 1kg pulverizing is got as aggregate, for subsequent use;
2) 30% aqueous solution of 10g carboxy-methyl hydroxy propyl guanidine glue is added under normal temperature, Homogeneous phase mixing;
3) by above-mentioned steps 2) in dry, the screening of mixture, to obtain final product.
Comparative example 3
Propping agent: patent CN1640981A, precoated sand prepared by the method for embodiment 2.
The settling velocity of embodiment 6-8, comparative example 3 propping agent in table 3 natural water
Embodiment 9
1) 40-70 order 1kg aluminium alloy spheroidal particle is got as aggregate, for subsequent use;
2) 30% aqueous solution of 10g carboxy-methyl hydroxy propyl guanidine glue is added under normal temperature, Homogeneous phase mixing;
3) by above-mentioned steps 2) in dry, the screening of mixture, to obtain final product.
Embodiment 10
1) 40-70 order 1kg glass microsphere is got as aggregate, for subsequent use;
2) 40% aqueous solution of hydroxypropyl guar 6g is added under normal temperature, Homogeneous phase mixing;
3) by above-mentioned steps 2) in dry, the screening of mixture, to obtain final product.
Embodiment 11
1) 20-40 order 1kg stainless steel particle is got as aggregate, for subsequent use;
2) be heated to 180 DEG C, when temperature is down to 130 DEG C, add polymaleic anhydride (molecular weight 800) 10g, Homogeneous phase mixing;
3) by above-mentioned steps 2) in dry, the screening of mixture, to obtain final product.
Embodiment 12
1) 40-70 order 1kg bauxitic clay haydite and each half of sintered bauxite is got as aggregate, for subsequent use;
2) be heated to 180 DEG C, when temperature is down to 130 DEG C, add the mixed aqueous solution 20mL of polyacrylic acid 5g and polymaleic anhydride (molecular weight 800) 5g, Homogeneous phase mixing;
3) by above-mentioned steps 2) in dry, the screening of mixture, to obtain final product.
Test example 1
The water of the Repone K of the anionic polyacrylamide (molecular weight 3,000,000) of active water: 0.25g, OP-10,10g of 1g, 0.1g formaldehyde and 488.65g.
The preparation process of active water is: be dissolved in the water of 488.65g by the polyacrylamide of above-mentioned specified quantitative, mix, obtain viscous water; The OP-10 of above-mentioned specified quantitative is dissolved in the viscous water of acquisition, mixes; Add 10g Repone K again, stir; Add 0.1g formaldehyde, stir.
Clear water: tap water
Test method: the propping agent of embodiment 1-12, comparative example 1-3 has been carried out to liquid viscosity respectively, taken grittiness energy and frictional resistance parameter testing in active water, and viscosity determining procedure is see standard (SYT5107-2005); Settling velocity measures and adopts 0.5m plexi-glass tubular, and the active water that loading 45cm is high and sand, than the propping agent being 30%, shake up the settling velocity of test propping agent; Frictional resistance adopts DV-III viscometer, and configure the pressure break system of 30% sand ratio, fixed rotating speed and rotor, the moment of torsion measuring them characterizes.Test result is as following table 1-table 3:
Table 4 adds the viscosity of active water after propping agent
In table 4, the volume ratio of propping agent and active water is 30:100.Sequence number 1,2 ... represent embodiment 1, embodiment 2 ...., sequence number " to 1 " represents comparative example 1.Lower same.
The settling velocity of propping agent in table 5 active water
The frictional resistance of propping agent in table 6 active water
Test result shows, and what the present invention proposed has excellent prop-carrying capacity from suspended prop and fall frictional resistance ability in active water.
Test method: to embodiment 1,4,6, the propping agent of 9-12, comparative example 1-3 carried out liquid viscosity respectively, taken grittiness energy and frictional resistance parameter testing in clear water, viscosity determining procedure is see standard (SYT5107-2005); Settling velocity measures and adopts 0.5m plexi-glass tubular, and the active water that loading 45cm is high and sand, than the propping agent being 30%, shake up the settling velocity of test propping agent; Frictional resistance adopts DV-III viscometer, and configure the pressure break system of 30% sand ratio, fixed rotating speed and rotor, the moment of torsion measuring them characterizes.Test result is as following table 7:
Table 7 adds the viscosity of clear water after propping agent
Propping agent prepared by the embodiment of the present application 1-10, joins in clear water according to sand ratio (volume ratio of propping agent and water) 10:100,20:100,30:100, after stirring, all can suspend more than two hours.
The propping agent of comparative example, joins in clear water according to sand ratio (volume ratio of propping agent and water) 10:100,20:100,30:100, after stirring, and quartz sand about 10 seconds sedimentation 0.5m, haydite about 15 seconds, precoated sand about 30 seconds.
Experimental example 2
With reference to People's Republic of China's oil and gas industry standard, fracturing propping agents filling bed short-term flow conductivity evaluation method, namely APIRP61 tests rate of permeation, the mechanical property of different propping agent packing layer.The results are shown in Table 8, table 9.
The each test group permeability result of table 8 (unit: μm
2.cm)
Carry out mechanical property detection according to standard SY/T5108-2006, the group name of each experimental group is the same, and detected result is in table 9:
Table 9 mechanical strength test
Above embodiment is only be described the preferred embodiment of the present invention; not scope of the present invention is limited; under not departing from the present invention and designing the prerequisite of spirit; the various modification that the common engineering technical personnel in this area make technical scheme of the present invention and improvement, all should fall in protection domain that claims of the present invention determine.
Claims (9)
1. from a preparation method for suspended prop, it is characterized in that, is under 15-150 DEG C of condition, is scattered in by water-soluble high-molecular material in aggregate obtained;
Described water-soluble high-molecular material is selected from the macromolecular material of natural polymer, synthetic polymer or half-natural semi-artificial synthesis, and the consumption of described water-soluble high-molecular material is 0.1 ~ 15wt% of aggregate consumption.
2. preparation method according to claim 1, it is characterized in that, described aggregate is one or more in the shell particle of quartz sand, haydite, metallic particles, globular glass particle, sintered bauxite, sintered alumina, sintered zirconia, synthetic resins, precoated sand, pulverizing; Described aggregate is of a size of 6-200 order.
3. preparation method according to claim 2, is characterized in that, the material of described metallic particles is one or more in carbon steel, stainless steel, aluminium alloy, iron-nickel alloy, Ferro Manganese.
4. preparation method according to claim 1, is characterized in that, described natural macromolecular material is selected from vegetable jelly, gelatin or microbiological gum; Described vegetable jelly is one or more in gum arabic, tragacanth gum, locust bean gum, guanidine glue, sesbania gum, rubber made from soybean cake; Described gelatin is one or more in gelatine, gelatin, casein food grade, chitosan; Described microbiological gum be selected from xanthan gum, gelling gum, curdlan one or more;
The macromolecular material of described synthetic comprises condensation class and polymeric type macromolecular material; Wherein, condensation family macromolecule material is selected from one or more in versamid 900, aminoresin and urethane resin; Polymeric type macromolecular material be selected from polyacrylamide, polyacrylic acid, polyoxyethylene glycol, polyoxyethylene, polymaleic anhydride, polyquaternium one or more;
The macromolecular material of described half-natural semi-artificial synthesis comprises treated starch, modified-cellulose and modified plant gum, is specifically selected from one or more in carboxymethyl cellulose, Walocel MT 20.000PV, methylcellulose gum, ethyl cellulose, Natvosol, propyloic starch, starch acetates, methylol guar gum, hydroxypropylguar gum, Carboxymethyl hydroxypropyl guar.
5. according to the arbitrary described preparation method of claim 1-4, it is characterized in that, be under 15-60 DEG C of condition, is scattered in by water-soluble high-molecular material in aggregate obtained;
Described water-soluble high-molecular material is selected from the one in vegetable jelly, gelatin or microbiological gum, and the consumption of described water-soluble polymer is the 0.5-15wt% of aggregate consumption.
6. according to the arbitrary described preparation method of claim 1-4, it is characterized in that, be under 80-150 DEG C of condition, is scattered in by water-soluble high-molecular material in aggregate obtained;
Described water-soluble high-molecular material be selected from polyacrylamide, polyacrylic acid, polyoxyethylene glycol, polyoxyethylene, polymaleic anhydride, polyquaternium, carboxymethyl cellulose, Walocel MT 20.000PV, methylcellulose gum, ethyl cellulose, Natvosol, propyloic starch, starch acetates, methylol guar gum, hydroxypropylguar gum, Carboxymethyl hydroxypropyl guar one or more;
The consumption of described water-soluble high-molecular material is the 0.1-15wt% of aggregate consumption.
7. preparation method according to claim 5, is characterized in that, also comprises the step of drying, screening.
8. preparation method according to claim 6, is characterized in that, is aggregate is first warming up to 170-200 DEG C, then treats that aggregate is cooled to 80-150 DEG C, is scattered in aggregate by water-soluble high-molecular material.
9. the arbitrary described preparation method of claim 1-8 prepare from suspended prop.
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CN201410124452.0A CN104946235A (en) | 2014-03-28 | 2014-03-28 | Preparation method of self-suspension proppant and prepared proppant |
CA2948953A CA2948953A1 (en) | 2014-03-28 | 2015-03-27 | Self-suspending proppant and preparation and use thereof |
PCT/CN2015/075289 WO2015144091A1 (en) | 2014-03-28 | 2015-03-27 | Self-suspending proppant and preparation and use thereof |
US15/129,773 US20170145302A1 (en) | 2014-03-28 | 2015-03-27 | Self-suspending proppant and preparation and use thereof |
RU2016142542A RU2652592C1 (en) | 2014-03-28 | 2015-03-27 | Self-advancing proppant, its preparation and usage |
EP15769703.8A EP3124741A4 (en) | 2014-03-28 | 2015-03-27 | Self-suspending proppant and preparation and use thereof |
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