CN105586027A - Preparation method of shale gas production fracturing propping agent - Google Patents
Preparation method of shale gas production fracturing propping agent Download PDFInfo
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- CN105586027A CN105586027A CN201610152275.6A CN201610152275A CN105586027A CN 105586027 A CN105586027 A CN 105586027A CN 201610152275 A CN201610152275 A CN 201610152275A CN 105586027 A CN105586027 A CN 105586027A
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Abstract
The invention discloses a preparation method of a shale gas production fracturing propping agent. The agent is prepared from, by weight, 20-30 parts of alunite expanding agent, 20-30 parts of calcium oxide expanding agent, 70-85 parts of kaoline, 5-10 parts of bentonite, 5-10 parts of quartz, 3-5 parts of feldspar, 2-3 parts of carbonate mineral, 1-3 parts of zinc oxide whisker and 1-3 parts of tertiary calcium phosphate. Through the continuous dry grinding process and the continuous wet grinding process, material uniformity is improved; through a compound sintering aid, solid-phase sintering is promoted; by controlling the heat-preservation sintering mode of ball blanks at different parts of a mechanical shaft kiln or a rotary kiln, the formation of long columnar mullite is promoted, and the content of columnar mullite in a product reaches 70-80%.
Description
Technical field
The present invention relates to a kind of shale gas exploitation field, be specifically related to a kind of for exploiting the system of shale gas fracturing propping agentsPreparation Method.
Background technology
Shale gas fracturing technique is to extrude crack by fracturing fluid to stratum shale, is the mobile passage of opening of shale gas,Prevent crack closure under formation closure pressure condition, need to use fracturing propping agents. Fracturing propping agents enter stratum with fracturing fluidShale gap, resident in the gap forming at fracturing fluid, stopping the closure in shale crack, form a high flow conductivitySupport belt. Therefore, fracturing propping agents are to affect the critical material that shale gas exploitation is collected. In the exploitation of oil, conventional gasIn process, also can use proppant, but because oil, conventional gas are present in discrete rock, clossing pressure is low, spaceRelatively many, so not high to the requirement of fracturing propping agents. But in the exploitation of shale gas, shale is fine and close aggregation,The gap that fracturing fluid forms is easy under high clossing pressure closed, and it is non-that the collection shale gas of gathering is split in the space of therefore supporting shaleOften important, require proppant to there is high strength to avoid shale gap closure.
Shale gas is exploited fracturing propping agents used and is mainly quartz sand and ceramic particle at present. The pressure-bearing of general quartz sandAbility is at 35MPa, percentage of damage≤10%; The bearing capacity 52MPa of ceramic particle, percentage of damage≤25%; 69MPa, percentage of damage≤ 20%; And the closing force of deep layer shale can reach 100MPa, common quartz sand and ceramic particle are difficult to reach shale exploitationIn support strength requirement. In addition, haydite materials mainly adopts bauxite, and production cost is too high, and resource is rare gradually, largeScale utilizes bauxite to prepare haydite to be subject to for shale gas exploitation the restriction of bauxite resource.
Summary of the invention
Object of the present invention is to overcome the deficiencies in the prior art, provides a kind of for exploiting shale gas fracturing propping agentsPreparation method.
Of the present invention being achieved through the following technical solutions: a kind of for exploiting the preparation method of shale gas fracturing propping agents,It is characterized in that:
(1) raw material and weight portion: alumite plumping agent 20-30 part, calcium oxide swelling agent 20-30 part, kaolin 70-85Part, bentonite 5-10 part, quartzy 5-10 part, feldspar 3-5 part, carbonate mineral 2-3 part, ZnOw 1-3Part, tricalcium phosphate 1-3 part;
(2) dry grinding continuously: the raw material that step (1) is prepared packs continuous dry method ball mill ball milling into by automatical feeding system,Cross 200 mesh sieves, obtain expecting powder; Milling parameters is: taking stainless steel ball as abrasive media, and the quality of raw material and stainless steel ballThan being 1:5~3;
(3) continuous wet-grinding: step (2) gained powder is sent into continuous wet-grinding machine by automatical feeding system and carry out continuous wet-grindingReach 5~20 microns to mud granularity, then send into the old 24 ± 2h of mud pit; Milling parameters is: with stainless steelBall is abrasive media, and the mass ratio of raw material, stainless steel ball and water is 1:2.5~3.5:0.5;
(4) mist projection granulating: the mud after old step (3) is pumped into spray drying tower and carry out drying-granulating, obtain water contentIt is 0.1~0.5% discrete particles;
(5) powder material scattering: use the equipment of breaing up that the discrete particles of step (4) gained is broken up again as grain after continuous wet-grindingThe powder in footpath;
(6) step (5) gained powder being obtained to granularity through nodulizer rolling is the spherical base substrate of 20-40 object proppant;
(7) the spherical base substrate of proppant step (6) being obtained is dry 30 ± 2h at 120~140 DEG C of temperature, then existsIn cement mechanized shaft kiln or rotary kiln, fire and obtain the special fracturing propping agents of the high-intensity shale gas of extremely-low density.
Further, described step (7) fires in cement mechanized shaft kiln that to obtain the high-intensity shale gas of extremely-low density specialWith fracturing propping agents; In cement mechanized shaft kiln with the firing rate of 8~25 DEG C/min from room temperature be warming up to 1200~1350 DEG C are burnt till, and insulation 2~6h, is wherein incubated 1h 800 DEG C time, is incubated 1h 1000 DEG C time; Again with 25~45 DEG C/The cooling velocity cooling of min.
Further, described step (7) is fired and is obtained the special pressure break of the high-intensity shale gas of extremely-low density in rotary kilnProppant; The rotating speed of described rotary kiln is 2-5 rev/min, and the highest firing temperature is 1380-1420 DEG C.
The present invention compared with prior art, has following advantage and beneficial effect:
1, the present invention is dry grinded and is improved material uniformity, urgees by complex sintering aids with continuous type wet grinding process by continous wayEnter solid-phase sintering; Jointly promote long by controlling ball base at the firing mode of mechanical type shaft kiln or the insulation of rotary kiln different partsThe formation of rod-like mullite, in product, the content of rod-like mullite reaches 70-80%.
2, the present invention adopts continous way dry method ball milling to add wet-grinding technology and relative device, guarantees uniformity, the stability of each raw material in slurry,Improved grinding efficiency, employing equipment is few, and floor space is few, has reduced cost of investment, can also serialization produce energy consumption simultaneouslyLittle; Adopt the stainless steel ball that quality is large is abrasive media simultaneously, improves grinding efficiency.
3, special fracturing propping agents of shale gas of the present invention and preparation method thereof utilize ready-made ripe device fabrication, without increaseOther equipment investments, can produce the special fracturing propping agents of high-performance shale gas with lower cost, have significant societyBenefit, environmental benefit, economic benefit.
Brief description of the drawings
Accompanying drawing described herein is used to provide the further understanding to the embodiment of the present invention, forms of the applicationPoint, do not form the restriction to the embodiment of the present invention. In the accompanying drawings:
Fig. 1 is the embodiment of the present invention 1 pressure and the broken rate test intention that falls;
Fig. 2 is the embodiment of the present invention 2 pressure and the broken rate test intention that falls.
Detailed description of the invention
For making the object, technical solutions and advantages of the present invention clearer, below in conjunction with embodiment and accompanying drawing, to thisInvention is described in further detail, and exemplary embodiment of the present invention and explanation thereof, only for explaining the present invention, are not doneFor limitation of the invention.
Embodiment 1
For exploiting a preparation method for shale gas fracturing propping agents, it is characterized in that:
(1) raw material and weight portion: 20 parts of alumite plumping agents, 20 parts of calcium oxide swelling agents, 70 parts of kaolin, bentonite 5Part, 5 parts, quartz, 3 parts of feldspars, 2 parts of carbonate minerals, 1 part of ZnOw, 1 part of tricalcium phosphate;
(2) dry grinding continuously: the raw material that step (1) is prepared packs continuous dry method ball mill ball milling into by automatical feeding system,Cross 200 mesh sieves, obtain expecting powder; Milling parameters is: taking stainless steel ball as abrasive media, and the matter of raw material and stainless steel ballAmount is than being 1:5;
(3) continuous wet-grinding: step (2) gained powder is sent into continuous wet-grinding machine by automatical feeding system and carry out continuous wet-grindingReach 5 microns to mud granularity, then send into mud pit old 24; Milling parameters is: taking stainless steel ball as grinding mediumMatter, the mass ratio of raw material, stainless steel ball and water is 1:2.5;
(4) mist projection granulating: the mud after old step (3) is pumped into spray drying tower and carry out drying-granulating, obtain water contentIt is 0.1 discrete particles;
(5) powder material scattering: use is broken up equipment the discrete particles of step (4) gained is broken up again as after continuous wet-grindingThe powder of particle diameter;
(6) step (5) gained powder being obtained to granularity through nodulizer rolling is the spherical base substrate of 20 object proppant;
(7) the spherical base substrate of proppant step (6) being obtained is dried 30 at 120 temperature, then at cement mechanized shaft kilnOr in rotary kiln, fire and obtain the special fracturing propping agents of the high-intensity shale gas of extremely-low density.
Described step (7) is fired and is obtained the special pressure break support of the high-intensity shale gas of extremely-low density in cement mechanized shaft kilnAgent; In cement mechanized shaft kiln, be warming up to 1200 DEG C with the firing rate of 8 DEG C/min from room temperature and burn till, insulation 2h, itsIn be incubated 1h 800 DEG C time, 1000 DEG C time, be incubated 1h; Lower the temperature with the cooling velocity of 25 DEG C/min again.
Described step (7) is fired and is obtained the special fracturing propping agents of the high-intensity shale gas of extremely-low density in rotary kiln; InstituteThe rotating speed of stating rotary kiln is 2 revs/min, and the highest firing temperature is 1380 DEG C. Sample test by embodiment 1 is obtained: bodyLong-pending density is that 1.33g/cm3, apparent density are 2.26g/cm3; Microsphere particle circularity is greater than 0.95, and sphericity is greater than 0.95; By sampleProduct adopt respectively dry method and bowssening test percentage of damage under 86MPa, 100MPa, the high clossing pressure of 120MPa, test result asAccompanying drawing 1:
By test analysis, the present embodiment sample with the immersion of the aqueous fluid such as fracturing fluid after, after water infiltrates proppant kernel byCause the compressive resistance of proppant and crush resistance significantly to promote in microdilatancy stress, and along with clossing pressure rising percentage of damage increasesAdduction is not obvious, is particularly useful for the exploitation of shale gas pressure break or the ultradeep well natural gas extraction of the high clossing pressure of 100MPa.
Embodiment 2
For exploiting a preparation method for shale gas fracturing propping agents, it is characterized in that:
(1) raw material and weight portion: 30 parts of alumite plumping agents, 30 parts of calcium oxide swelling agents, 85 parts of kaolin, bentonite 10Part, 10 parts, quartz, 5 parts of feldspars, 3 parts of carbonate minerals, 3 parts of ZnOws, 3 parts of tricalcium phosphates;
(2) dry grinding continuously: the raw material that step (1) is prepared packs continuous dry method ball mill ball milling into by automatical feeding system,Cross 200 mesh sieves, obtain expecting powder; Milling parameters is: taking stainless steel ball as abrasive media, and the quality of raw material and stainless steel ballThan being 1:5~3;
(3) continuous wet-grinding: step (2) gained powder is sent into continuous wet-grinding machine by automatical feeding system and carry out continuous wet-grindingReach 20 microns to mud granularity, then send into the old 26h of mud pit; Milling parameters is: taking stainless steel ball as grinding mediumMatter, the mass ratio of raw material, stainless steel ball and water is 3.5:0.5;
(4) mist projection granulating: the mud after old step (3) is pumped into spray drying tower and carry out drying-granulating, obtain water contentIt is 0.5% discrete particles;
(5) powder material scattering: use is broken up equipment the discrete particles of step (4) gained is broken up again as after continuous wet-grindingThe powder of particle diameter;
(6) step (5) gained powder being obtained to granularity through nodulizer rolling is the spherical base substrate of 40 object proppant;
(7) the spherical base substrate of proppant step (6) being obtained is dry 32h at 140 DEG C of temperature, then vertical at cement machineryIn kiln or rotary kiln, fire and obtain the special fracturing propping agents of the high-intensity shale gas of extremely-low density.
Described step (7) is fired and is obtained the special pressure break support of the high-intensity shale gas of extremely-low density in cement mechanized shaft kilnAgent; In cement mechanized shaft kiln, be warming up to 1350 DEG C with the firing rate of 25 DEG C/min from room temperature and burn till, insulation 6h, itsIn be incubated 1h 800 DEG C time, 1000 DEG C time, be incubated 1h; Lower the temperature with the cooling velocity of 45 DEG C/min again.
Described step (7) is fired and is obtained the special fracturing propping agents of the high-intensity shale gas of extremely-low density in rotary kiln;The rotating speed of described rotary kiln is 2-5 rev/min, and the highest firing temperature is 1420 DEG C. Survey by the sample that embodiment 2 is obtainedExamination: bulk density is that 1.41g/cm3, apparent density are 2.32g/cm3; Microsphere particle circularity is greater than 0.95, and sphericity is greater than 0.95; Sample is adopted respectively under 86MPa, 100MPa, the high clossing pressure of 120MPa to dry method and bowssening test percentage of damage, testResult is as accompanying drawing 2:
By test analysis, the present embodiment sample with the immersion of the aqueous fluid such as fracturing fluid after, after water infiltrates proppant kernel byCause the compressive resistance of proppant and crush resistance significantly to promote in microdilatancy stress, and along with clossing pressure rising percentage of damage increasesAdduction is not obvious, is particularly useful for the exploitation of shale gas pressure break or the ultradeep well natural gas extraction of the high clossing pressure of 100MPa.
Above-described detailed description of the invention, has carried out further object of the present invention, technical scheme and beneficial effectDescribe in detail, institute it should be understood that and the foregoing is only the specific embodiment of the present invention, is not intended to limit the present inventionProtection domain, within the spirit and principles in the present invention all, any amendment of making, be equal to replacement, improvement etc., all should compriseWithin protection scope of the present invention.
Claims (3)
1. for exploiting a preparation method for shale gas fracturing propping agents, it is characterized in that:
(1) raw material and weight portion: alumite plumping agent 20-30 part, calcium oxide swelling agent 20-30 part, kaolin 70-85Part, bentonite 5-10 part, quartzy 5-10 part, feldspar 3-5 part, carbonate mineral 2-3 part, ZnOw 1-3Part, tricalcium phosphate 1-3 part;
(2) dry grinding continuously: the raw material that step (1) is prepared packs continuous dry method ball mill ball milling into by automatical feeding system,Cross 200 mesh sieves, obtain expecting powder; Milling parameters is: taking stainless steel ball as abrasive media, and the quality of raw material and stainless steel ballThan being 1:5~3;
(3) continuous wet-grinding: step (2) gained powder is sent into continuous wet-grinding machine by automatical feeding system and carry out continuous wet-grindingReach 5~20 microns to mud granularity, then send into the old 24 ± 2h of mud pit; Milling parameters is: with stainless steel ballFor abrasive media, the mass ratio of raw material, stainless steel ball and water is 1:2.5~3.5:0.5;
(4) mist projection granulating: the mud after old step (3) is pumped into spray drying tower and carry out drying-granulating, obtain water contentIt is 0.1~0.5% discrete particles;
(5) powder material scattering: use is broken up equipment the discrete particles of step (4) gained is broken up again as particle diameter after continuous wet-grindingPowder;
(6) step (5) gained powder being obtained to granularity through nodulizer rolling is the spherical base substrate of 20-40 object proppant;
(7) the spherical base substrate of proppant step (6) being obtained is dry 30 ± 2h at 120~140 DEG C of temperature, then existsIn cement mechanized shaft kiln or rotary kiln, fire and obtain the special fracturing propping agents of the high-intensity shale gas of extremely-low density.
2. according to claim 1 a kind ofly it is characterized in that for exploiting the preparation method of shale gas fracturing propping agents, instituteState step (7) fires and obtains the special fracturing propping agents of the high-intensity shale gas of extremely-low density in cement mechanized shaft kiln; At cementIn mechanical vertical kiln, be warming up to 1200~1350 DEG C with the firing rate of 8~25 DEG C/min from room temperature and burn till, insulation 2~6h, is wherein incubated 1h 800 DEG C time, is incubated 1h 1000 DEG C time; Lower the temperature with the cooling velocity of 25~45 DEG C/min again.
3. according to claim 1 a kind of for exploiting the preparation method of shale gas fracturing propping agents, it is characterized in that:Described step (7) is fired and is obtained the special fracturing propping agents of the high-intensity shale gas of extremely-low density in rotary kiln; Described rotary kilnRotating speed be 2-5 rev/min, the highest firing temperature is 1380-1420 DEG C.
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CN108120820A (en) * | 2017-12-20 | 2018-06-05 | 四川圣诺油气工程技术服务有限公司 | A kind of method of shale gas pressure break quality control |
CN110354970A (en) * | 2018-04-10 | 2019-10-22 | 中国石油天然气股份有限公司 | A kind of processing method of shale gas pressure break river sand proppant |
CN114015431A (en) * | 2021-12-07 | 2022-02-08 | 河南郑矿机器有限公司 | Low-density petroleum ceramsite proppant and preparation method thereof |
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CN103172354A (en) * | 2013-04-15 | 2013-06-26 | 金刚新材料股份有限公司 | Preparation method of fracturing propping agent for exploiting shale gas |
CN103773355A (en) * | 2014-01-15 | 2014-05-07 | 成都新柯力化工科技有限公司 | Fracturing propping agent for shale gas mining and preparation method thereof |
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CN103172354A (en) * | 2013-04-15 | 2013-06-26 | 金刚新材料股份有限公司 | Preparation method of fracturing propping agent for exploiting shale gas |
CN103773355A (en) * | 2014-01-15 | 2014-05-07 | 成都新柯力化工科技有限公司 | Fracturing propping agent for shale gas mining and preparation method thereof |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN108120820A (en) * | 2017-12-20 | 2018-06-05 | 四川圣诺油气工程技术服务有限公司 | A kind of method of shale gas pressure break quality control |
CN110354970A (en) * | 2018-04-10 | 2019-10-22 | 中国石油天然气股份有限公司 | A kind of processing method of shale gas pressure break river sand proppant |
CN114015431A (en) * | 2021-12-07 | 2022-02-08 | 河南郑矿机器有限公司 | Low-density petroleum ceramsite proppant and preparation method thereof |
CN114015431B (en) * | 2021-12-07 | 2023-01-31 | 河南郑矿机器有限公司 | Low-density petroleum ceramsite proppant and preparation method thereof |
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