CN109536158A - A kind of low-density ceramic proppant and preparation method thereof - Google Patents

A kind of low-density ceramic proppant and preparation method thereof Download PDF

Info

Publication number
CN109536158A
CN109536158A CN201710862659.1A CN201710862659A CN109536158A CN 109536158 A CN109536158 A CN 109536158A CN 201710862659 A CN201710862659 A CN 201710862659A CN 109536158 A CN109536158 A CN 109536158A
Authority
CN
China
Prior art keywords
haydite
low
initiator
high molecular
preparation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201710862659.1A
Other languages
Chinese (zh)
Other versions
CN109536158B (en
Inventor
陈培胜
陈勇
陈凯
李明
姜亦栋
郁登朗
丁然
王丽萍
张军峰
陈磊
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China Petroleum and Chemical Corp
Sinopec Research Institute of Petroleum Engineering Shengli Co
Original Assignee
China Petroleum and Chemical Corp
Sinopec Research Institute of Petroleum Engineering Shengli Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by China Petroleum and Chemical Corp, Sinopec Research Institute of Petroleum Engineering Shengli Co filed Critical China Petroleum and Chemical Corp
Priority to CN201710862659.1A priority Critical patent/CN109536158B/en
Publication of CN109536158A publication Critical patent/CN109536158A/en
Application granted granted Critical
Publication of CN109536158B publication Critical patent/CN109536158B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/80Compositions for reinforcing fractures, e.g. compositions of proppants used to keep the fractures open
    • C09K8/805Coated proppants

Abstract

The invention discloses a kind of low-density ceramic proppant, preparation methods are as follows: (1) part haydite materials with high molecular polymer microballoon are mixed, it is spraying to soak, and it stands, balling-up of pelletizing;(2) haydite materials of surplus are added, continue to pelletize;(3) 300 DEG C are warming up to, be then sintered at 1300~1400 DEG C to get.High molecular polymer microballoon is prepared from the following raw materials: tasteless kerosene or white oil 20%~30%, emulsifier 3%~12%, acrylamide 5%~30%, acrylic acid 5%~30%, N, N- methene base bisacrylamide 3%~7%, initiator 0.01%~0.1%, surplus are water.Ceramsite propping agent of the invention, density is in 1.8~2.0g/cm3Average grain diameter 0.83mm, compressive resistance with higher (inside the hollow ball uniform pack haydite of rule, can be effectively reduced haydite density, its original compression strength is maintained to greatest extent), it can be used as fracture in oil and water wells and applied with proppant.

Description

A kind of low-density ceramic proppant and preparation method thereof
Technical field
The present invention relates to a kind of low-density ceramic proppant and preparation method thereof, and as fracture in oil and water wells proppant In application.
Background technique
Deep-seated oil, gas well are developed, yield is improved, fracturing technology is widely adopted.To ensure having for underground deep layer pressure-break Effect struts, suitable proppant be it is necessary, it can increase the flow conductivity on stratum, improve the yield of oil or gas, be pressure break work One key factor of skill application quality.Common fracturing propping agents domestic at present are quartz sand and haydite.Wherein quartz sand Cheap, relative density is low, and convenient for construction pumping, but the intensity of quartz sand is low, sphericity is poor, percentage of damage is high, to drop The low flow conductivity in crack, is not particularly well suited for the high deep-well of clossing pressure.For sintering ceramsite due to intensity height, sphericity is good, For the fracturing propping agents that people preferentially select, it is constantly subjected to pay much attention to.
The density of conventional proppants is larger, easily settles to form whaleback near wellbore in pressure break pumping procedure, finally have Effect supporting crack is shorter, and the oil-gas reservoir volume of communication is less, and to improving, oil well output is unfavorable.When proppant density is smaller, splitting Laid in seam it is more uniform, effectively support seam it is longer.Therefore, reducing proppant density becomes the Main way of proppant development.
Super-low-density proppant refers to apparent density less than 2.0 at present, other performances meet the proppant of pressing crack construction requirement. Two classes: inorganic material proppant, including hollow haydite, porous ceramic grain, hollow glass micro-ball etc. are broadly divided into, its advantage is that resistance to Temperature, but intensity contrast solid support agent reduction is larger, limits application.Organic material proppant, including resin coating haydite and High molecular polymer proppant, its advantage is that density is lower, but heat resisting and pressure resisting is inadequate, there is a small amount of application in shallow-layer pressure break.
Summary of the invention
For the above-mentioned prior art, the present invention provides a kind of low-density, high-strength ceramic proppant, the present invention also provides Preparation method.
The present invention is achieved by the following technical solutions:
A kind of preparation method of low-density ceramic proppant, comprising the following steps:
(1) haydite materials and high molecular polymer microballoon of haydite materials total amount 78%~81% (preferably 79.5%) will be accounted for The volume ratio of mixing, the haydite materials (referring to total amount) and high molecular polymer microballoon is 2.8~3.2:1, wherein being excellent with 3:1 Scheme is selected, is soaked by spraying in mixing, stands 10 hours after wetting, be placed in sugar coating machine balling-up of pelletizing, spherolite to be averaged later After diameter reaches 0.78mm, drying 24 hours is taken out, semi-finished product are obtained;
(2) semi-finished product are placed in sugar coating machine, be added surplus haydite materials (the 19%~22% of haydite materials total amount, In with 20.5% be optimal case), continue to pelletize (purpose is the high molecular polymer micro-spheres surface), it is to be averaged After partial size reaches 0.83mm, drying 24 hours is taken out, precast ceramsite is obtained;
(3) precast ceramsite is preheated, is warming up to 300 DEG C ± 20 DEG C, heating rate control 20~30 DEG C/it is small When, to ensure high molecular polymer slowly decomposition gasification, the hole left is the sphere of rule;After preheating, it is placed in sintering machine Be sintered, 1300~1400 DEG C of sintering temperature to get.
The haydite materials refer to the general raw material of manufacture haydite, can be selected from bauxite, kaolin, industrial waste (such as red mud Flyash, ceramic rod waste material etc.), preferred bauxite.
The high molecular polymer microballoon, partial size be 40~60 μm, 50 μm of average grain diameter, density 0.8g/cm3, be by Made of the raw material of following weight percent: tasteless kerosene or white oil 20%~30%, emulsifier 3%~12%, acrylamide 5%~30%, acrylic acid 5%~30%, N, N- methene base bisacrylamide 3%~7%, initiator 0.01%~0.1% is remaining Amount is water (preferably deionized water);It is prepared by the following method to obtain:
1. emulsion polymerization prepares microsphere precursor: removing each raw material outside initiator, mix, strong stirring 30min, addition is drawn Agent is sent out, is caused at 8 DEG C, fully reacting after 6h obtains polymer emulsion, is milky or translucent flowable liquids, polymer Effective content 30%~40%;
The emulsifier is conven-tional adjuvants in the prior art, can be selected from alkyl phenol polyoxyethylene ether (TX, OP series), rouge Fat alcohol polyoxyethylene ether (MOA series), isomery fatty alcohol polyoxyethylene ether, carboxylate fatty alcohol, carboxylate fatty amine, sulfate Fatty alcohol, sulfate fatty amine, sulfonate fatty alcohol, any one or two or more combinations in sulfonate fatty amine;
The initiator is radical initiator in the prior art, can be selected from azo-initiator (hot initiator system, packet Include: persulfate, water-soluble azo class), redox initiator (oxidation-reduction trigger system);It may make up redox body There are benzoyl peroxide/sucrose, tert-butyl hydroperoxide/rongalite, tert-butyl hydroperoxide/sodium pyrosulfite, peroxide in system Change benzoyl/n,N-Dimethylaniline, ammonium persulfate/sodium hydrogensulfite, potassium peroxydisulfate/sodium hydrogensulfite, hydrogen peroxide/winestone Acid, hydrogen peroxide/sodium formaldehyde sulfoxylate, ammonium persulfate/ferrous sulfate, hydrogen peroxide/sulfuric acid ferrous iron, benzoyl peroxide //N, N- diethyl Base aniline, benzoyl peroxide/ferrous pyrophosphate, potassium peroxydisulfate/silver nitrate, persulfate/mercaptan, isopropyl benzene hydroperoxide/ Frerrous chloride, potassium peroxydisulfate/frerrous chloride, hydrogen peroxide/frerrous chloride, isopropyl benzene hydroperoxide/tetra- aziridines etc.;
Preferably, it is made of the raw material of following weight percent: tasteless kerosene or white oil 25%, emulsifier 5%~ 8%, acrylamide 20%~30%, acrylic acid 5%~15%, N, N- methene base bisacrylamide 5%, initiator 0.01%~ 0.1%, surplus is water;
It is furthermore preferred that being made of the raw material of following weight percent: tasteless kerosene or white oil 25%, emulsifier 6%, Acrylamide 25%, acrylic acid 10%, N, N- methene base bisacrylamide 5%, initiator 0.01%~0.1%, surplus are to go Ionized water;
Preferably, the strong stirring refers to and stirs at 2000r/min;
2. polymer emulsion excess ethyl alcohol obtained above is deep, washing of precipitate 3~4 times, at 40 DEG C after powdered Drying is to get high molecular polymer microballoon is arrived, and 40~60 μm of particle diameter distribution, average grain diameter is 50 μm, density 0.8g/cm3, have Certain elasticity, circularity sphericity are high.
The low-density high-strength ceramic granule propping agent being prepared using the above method, density is in 1.8~2.0g/cm3, average Partial size 0.83mm, compressive resistance (resistance to compression 68MPa) with higher.
Low-density ceramic proppant of the invention can be used as fracture in oil and water wells and be applied with proppant.
Low-density ceramic proppant of the invention can be effectively inside the hollow ball uniform pack haydite of rule Haydite density is reduced, maintains its original compression strength to greatest extent.
Detailed description of the invention
Fig. 1: porous ceramic grain electromicroscopic photograph.
Fig. 2: solid haydite stress analysis schematic diagram.
Fig. 3: inside is the haydite stress analysis schematic diagram of regular circle shapes hole.
Fig. 4: inside there is the haydite stress analysis schematic diagram of irregular holes.
Fig. 5: concentrated stress and spherical hole number relational graph.
Specific embodiment
Below with reference to embodiment, the present invention is further illustrated.
Instrument involved in following embodiments, reagent, material etc. are unless otherwise noted existing in the prior art Conventional instrument, reagent, material etc., can be obtained by regular commercial sources.Experimental method involved in following embodiments, inspection Survey method etc. is unless otherwise noted existing routine experiment method in the prior art, detection method etc..
The development of 1 low-density ceramic proppant of embodiment
1, the reason of porous ceramic grain compressive resistance reduces:
The hole of porous ceramic grain is very irregular, and shape is varied, as shown in Figure 1, inside is easy to out in stress Existing stress is concentrated, and is caused to be crushed, is thus caused chain reaction, significantly reduces compressive resistance.
Force analysis: for solid haydite in pressure-resistant 65MPa, internal stress is 27MPa or so, stress concentration does not occur, As shown in Figure 2.When porous ceramic grain hole is regular circle shapes, pressure-resistant 65MPa, the stress that 75MPa occurs in inside is concentrated, and is such as schemed Shown in 3.When haydite inner void is irregular, pressure-resistant 65MPa will appear the stress collection of 170MPa in inner void irregularity In, it is broken so as to cause haydite, as shown in Figure 4.It can be seen that directly affecting haydite whether the hole rule of porous ceramic grain Compression strength.
2, low-density high-strength haydite invention thinking
Invention thinking: inside the hollow ball uniform pack haydite of rule, can be effectively reduced haydite density, maximum Its original compression strength of the maintenance of limit.By taking effective hollow volume accounts for the 1/3 of haydite total volume as an example, pressure-resistant 65MPa is carried out Finite element analysis has to draw a conclusion, as shown in table 1, Fig. 5.
Table 1
By table 1, Fig. 5 it is found that the spherical hole of porous ceramic grain is more, radius is smaller, then the stress of the inside of porous ceramic grain Concentrate it is smaller, so that the compressive resistance of porous ceramic grain is higher.
3, preparation method
Using bauxite as raw material (bulk density 1.7g/cm3), the solid haydite of the partial size 0.83mm of conventional method preparation, Its apparent density 2.7g/cm3, pressure-resistant 68MPa;As a comparison, high molecular polymer microballoon is filler, system using bauxite as raw material It is standby with the low-density ceramsite of partial size, identical compression strength, apparent density is down to 1.85g/cm3
Steps are as follows:
(1) high molecular polymer microballoon: raw material composition is prepared are as follows: white oil 25%, emulsifier 6%, acrylamide 25%, third Olefin(e) acid 10%, N, N- methene base bisacrylamide 5%, initiator 0.05%, surplus is deionized water;
1. emulsion polymerization prepares microsphere precursor: removing each raw material outside initiator, mix, 2000r/min strong stirring Initiator is added in 30min, causes at 8 DEG C, and fully reacting after 6h obtains polymer emulsion;
The emulsifier is emulsifier op-10;
The initiator is ammonium persulfate/sodium hydrogensulfite;
2. polymer emulsion excess ethyl alcohol obtained above is deep, washing of precipitate 4 times, at 40 DEG C of bakings after powdered It does to get high molecular polymer microballoon is arrived, 40~60 μm of particle diameter distribution, average grain diameter is 50 μm, density 0.8g/cm3, there is one Fixed elasticity, circularity sphericity are high.
(2) calculate the dosage of microballoon: compared with solid haydite, density reduces 1/3 (by 2.7g/cm3It is reduced to 1.85g/ cm3), then (bauxite bulk density is 1.7g/cm to haydite materials3) and polymer microballoon (density 0.8g/cm3) volume ratio be 3:1, reduced mass ratio are as follows: (explanation: bauxite needs to grind could carefully use 6.38:1 very much, and bulk density is after grinding 1.7g/cm3, the density of bauxite ore is very high).
Inner integrated stress can be found from Fig. 5 and is up to 57MPa or so, less than the broken pressure break of itself.
According to reduced density, then different raw materials will lead to the matter of different raw material and microballoon because density is different Amount ratio.
(3) haydite is prepared:
1. the haydite materials for accounting for haydite materials total amount 79.5% are mixed with high molecular polymer microballoon, it is sprayed in mixing Wetting, stands 10 hours after wetting, is placed in sugar coating machine balling-up of pelletizing later, after ball average grain diameter reaches 0.78mm, takes out It is 24 hours dry, obtain semi-finished product;
2. semi-finished product are placed in sugar coating machine, be added remaining haydite materials continue granulation (purpose is the macromolecule surface Polymer microballoon cladding is got up), after partial size to be averaged reaches 0.83mm, drying 24 hours is taken out, precast ceramsite is obtained;
3. preheating to precast ceramsite, 300 DEG C are warming up to, heating rate is controlled at 25 DEG C/h, to ensure high score Slowly decomposition gasification, the hole left are the sphere of rule to sub- polymer;After preheating, merging sintering machine is sintered, and is sintered 1350 DEG C of temperature to get.
Embodiment 2 prepares low-density ceramic proppant
Steps are as follows:
(1) high molecular polymer microballoon: raw material composition is prepared are as follows: white oil 25%, emulsifier 5%, acrylamide 30%, third Olefin(e) acid 5%, N, N- methene base bisacrylamide 5%, initiator 0.1%, surplus is deionized water;
1. emulsion polymerization prepares microsphere precursor: removing each raw material outside initiator, mix, 2000r/min strong stirring Initiator is added in 30min, causes at 8 DEG C, and fully reacting after 6h obtains polymer emulsion;
The emulsifier is isomery fatty alcohol polyoxyethylene ether;
The initiator is that hydrogen peroxide/sulfuric acid is ferrous;
2. polymer emulsion excess ethyl alcohol obtained above is deep, washing of precipitate 4 times, at 40 DEG C of bakings after powdered It does to get high molecular polymer microballoon is arrived.
(2) calculate the dosage of microballoon: the volume ratio of haydite materials (bauxite) and polymer microballoon is 3:1.
(3) haydite is prepared:
1. the haydite materials for accounting for haydite materials total amount 80% are mixed with high molecular polymer microballoon, moisten by spraying in mixing It is wet, 10 hours are stood after wetting, is placed in sugar coating machine balling-up of pelletizing later, after ball average grain diameter reaches 0.78mm, is taken out dry Dry 24 hours, obtain semi-finished product;
2. semi-finished product are placed in sugar coating machine, remaining haydite materials are added and continue to pelletize, partial size to be averaged reaches 0.83mm Afterwards, drying 24 hours is taken out, precast ceramsite is obtained;
3. preheating to precast ceramsite, 300 DEG C are warming up to, heating rate is controlled at 25 DEG C/h, to ensure high score Slowly decomposition gasification, the hole left are the sphere of rule to sub- polymer;After preheating, merging sintering machine is sintered, and is sintered 1350 DEG C of temperature to get.
Embodiment 3 prepares low-density ceramic proppant
Steps are as follows:
(1) high molecular polymer microballoon: raw material composition are as follows: tasteless kerosene 25%, emulsifier 8%, acrylamide is prepared 20%, acrylic acid 15%, N, N- methene base bisacrylamide 5%, initiator 0.02%, surplus is deionized water;
1. emulsion polymerization prepares microsphere precursor: removing each raw material outside initiator, mix, 2000r/min strong stirring Initiator is added in 30min, causes at 8 DEG C, and fully reacting after 6h obtains polymer emulsion;
The emulsifier is carboxylate fatty alcohol;
The initiator is potassium peroxydisulfate/frerrous chloride;
2. polymer emulsion excess ethyl alcohol obtained above is deep, washing of precipitate 4 times, at 40 DEG C of bakings after powdered It does to get high molecular polymer microballoon is arrived.
(2) calculate the dosage of microballoon: the volume ratio of haydite materials (bauxite) and polymer microballoon is 3:1.
(3) haydite is prepared:
1. the haydite materials for accounting for haydite materials total amount 78% are mixed with high molecular polymer microballoon, moisten by spraying in mixing It is wet, 10 hours are stood after wetting, is placed in sugar coating machine balling-up of pelletizing later, after ball average grain diameter reaches 0.78mm, is taken out dry Dry 24 hours, obtain semi-finished product;
2. semi-finished product are placed in sugar coating machine, remaining haydite materials are added and continue to pelletize, partial size to be averaged reaches 0.83mm Afterwards, drying 24 hours is taken out, precast ceramsite is obtained;
3. preheating to precast ceramsite, 300 DEG C are warming up to, heating rate is controlled at 25 DEG C/h, to ensure high score Slowly decomposition gasification, the hole left are the sphere of rule to sub- polymer;After preheating, merging sintering machine is sintered, and is sintered 1350 DEG C of temperature to get.
Embodiment 4 prepares low-density ceramic proppant
Steps are as follows:
(1) high molecular polymer microballoon: raw material composition is prepared are as follows: white oil 20%, emulsifier 12%, acrylamide 5%, third Olefin(e) acid 30%, N, N- methene base bisacrylamide 3%, initiator 0.08%, surplus is deionized water;
1. emulsion polymerization prepares microsphere precursor: removing each raw material outside initiator, mix, 2000r/min strong stirring Initiator is added in 30min, causes at 8 DEG C, and fully reacting after 6h obtains polymer emulsion;
The emulsifier is sulfate fatty alcohol;
The initiator is that hydrogen peroxide/sulfuric acid is ferrous;
2. polymer emulsion excess ethyl alcohol obtained above is deep, washing of precipitate 4 times, at 40 DEG C of bakings after powdered It does to get high molecular polymer microballoon is arrived.
(2) calculate the dosage of microballoon: the volume ratio of haydite materials (kaolin) and polymer microballoon is 3.2:1.
(3) haydite is prepared:
1. the haydite materials for accounting for haydite materials total amount 81% are mixed with high molecular polymer microballoon, moisten by spraying in mixing It is wet, 10 hours are stood after wetting, is placed in sugar coating machine balling-up of pelletizing later, after ball average grain diameter reaches 0.78mm, is taken out dry Dry 24 hours, obtain semi-finished product;
2. semi-finished product are placed in sugar coating machine, remaining haydite materials are added and continue to pelletize, partial size to be averaged reaches 0.83mm Afterwards, drying 24 hours is taken out, precast ceramsite is obtained;
3. preheating to precast ceramsite, 300 DEG C are warming up to, heating rate is controlled at 20 DEG C/h, to ensure high score Slowly decomposition gasification, the hole left are the sphere of rule to sub- polymer;After preheating, merging sintering machine is sintered, and is sintered 1300 DEG C of temperature to get.
Embodiment 5 prepares low-density ceramic proppant
Steps are as follows:
(1) high molecular polymer microballoon: raw material composition are as follows: tasteless kerosene 30%, emulsifier 3%, acrylamide is prepared 30%, acrylic acid 5%, N, N- methene base bisacrylamide 3%, initiator 0.01%, surplus is deionized water;
1. emulsion polymerization prepares microsphere precursor: removing each raw material outside initiator, mix, 2000r/min strong stirring Initiator is added in 30min, causes at 8 DEG C, and fully reacting after 6h obtains polymer emulsion;
The emulsifier is sulfonate fatty alcohol;
The initiator is isopropyl benzene hydroperoxide/frerrous chloride;
2. polymer emulsion excess ethyl alcohol obtained above is deep, washing of precipitate 3 times, at 40 DEG C of bakings after powdered It does to get high molecular polymer microballoon is arrived.
(2) calculate the dosage of microballoon: the volume ratio of haydite materials (red-mud coal ash) and polymer microballoon is 2.8:1.
(3) haydite is prepared:
1. the haydite materials for accounting for haydite materials total amount 79% are mixed with high molecular polymer microballoon, moisten by spraying in mixing It is wet, 10 hours are stood after wetting, is placed in sugar coating machine balling-up of pelletizing later, after ball average grain diameter reaches 0.78mm, is taken out dry Dry 24 hours, obtain semi-finished product;
2. semi-finished product are placed in sugar coating machine, remaining haydite materials are added and continue to pelletize, partial size to be averaged reaches 0.83mm Afterwards, drying 24 hours is taken out, precast ceramsite is obtained;
3. preheating to precast ceramsite, 300 DEG C are warming up to, heating rate is controlled at 30 DEG C/h, to ensure high score Slowly decomposition gasification, the hole left are the sphere of rule to sub- polymer;After preheating, merging sintering machine is sintered, and is sintered 1400 DEG C of temperature to get.
Above-mentioned, although specific embodiments of the present invention have been described in conjunction with the embodiments, not protects to the present invention The limitation of range, those skilled in the art should understand that, based on the technical solutions of the present invention, those skilled in the art The various modifications or changes that can be made are not needed to make the creative labor still within protection scope of the present invention.

Claims (10)

1. a kind of preparation method of low-density ceramic proppant, it is characterised in that: the following steps are included:
(1) haydite materials for accounting for haydite materials total amount 78%~81% are mixed with high molecular polymer microballoon, the haydite is former The volume ratio of material and high molecular polymer microballoon is 2.8~3.2:1, soaks by spraying in mixing, stands after wetting, be placed in later It pelletizes in sugar coating machine balling-up, takes out drying, obtain semi-finished product;
(2) semi-finished product are placed in sugar coating machine, the haydite materials of surplus is added, continue to pelletize, taken out drying, obtain precast ceramsite;
(3) precast ceramsite is preheated, is warming up to 300 DEG C ± 20 DEG C, heating rate is controlled at 20~30 DEG C/h;In advance After heating, merging sintering machine is sintered, 1300~1400 DEG C of sintering temperature to get;
The high molecular polymer microballoon is made of the raw material of following weight percent: tasteless kerosene or white oil 20%~ 30%, emulsifier 3%~12%, acrylamide 5%~30%, acrylic acid 5%~30%, N, N- methene base bisacrylamide 3%~7%, initiator 0.01%~0.1%, surplus is water;It is prepared by the following method to obtain:
1. emulsion polymerization prepares microsphere precursor: removing each raw material outside initiator, mix, stirring is added initiator, draws at 8 DEG C Hair, obtains polymer emulsion after fully reacting;
2. polymer emulsion excess ethyl alcohol is deep, it washing of precipitate 3~4 times, dries to get high molecular polymer microballoon is arrived.
2. the preparation method of low-density ceramic proppant according to claim 1, it is characterised in that: the haydite materials, Selected from bauxite, kaolin, industrial waste.
3. the preparation method of low-density ceramic proppant according to claim 1, it is characterised in that: in the step (1), The volume ratio of haydite materials and high molecular polymer microballoon is 3:1.
4. the preparation method of low-density ceramic proppant according to claim 1, it is characterised in that: in the step (1), The haydite materials for accounting for haydite materials total amount 79.5% are mixed with high molecular polymer microballoon.
5. the preparation method of low-density ceramic proppant according to claim 1, it is characterised in that: in the step (1), 10 hours are stood after wetting, is placed in sugar coating machine balling-up of pelletizing later, after spherolite diameter reaches 0.78mm, it is small to take out dry 24 When, obtain semi-finished product;
In the step (2), continue to pelletize, after partial size to be averaged reaches 0.83mm, takes out drying, obtain precast ceramsite.
6. the preparation method of low-density ceramic proppant according to claim 1, it is characterised in that: the high molecular polymerization Object microballoon is made of the raw material of following weight percent: tasteless kerosene or white oil 25%, emulsifier 5%~8%, propylene Amide 20%~30%, acrylic acid 5%~15%, N, N- methene base bisacrylamide 5%, initiator 0.01%~0.1% is remaining Amount is water.
7. the preparation method of low-density ceramic proppant according to claim 1, it is characterised in that: the high molecular polymerization Object microballoon is made of the raw material of following weight percent: tasteless kerosene or white oil 25%, emulsifier 6%, acrylamide 25%, acrylic acid 10%, N, N- methene base bisacrylamide 5%, initiator 0.01%~0.1%, surplus is deionized water.
8. the preparation method of low-density ceramic proppant according to claim 1, it is characterised in that: the emulsifier is selected from Alkyl phenol polyoxyethylene ether, fatty alcohol polyoxyethylene ether, isomery fatty alcohol polyoxyethylene ether, carboxylate fatty alcohol, carboxylate rouge Fat amine, sulfate fatty alcohol, sulfate fatty amine, sulfonate fatty alcohol, any one or two kinds in sulfonate fatty amine with On combination;
The initiator is selected from azo-initiator, redox initiator.
9. being prepared using the preparation method of low-density ceramic proppant described in any one of claim 1~8 low close Spend high-strength ceramic granule propping agent.
10. low-density ceramic proppant as claimed in claim 9 is as the application in fracture in oil and water wells proppant.
CN201710862659.1A 2017-09-21 2017-09-21 Low-density ceramsite proppant and preparation method thereof Active CN109536158B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710862659.1A CN109536158B (en) 2017-09-21 2017-09-21 Low-density ceramsite proppant and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710862659.1A CN109536158B (en) 2017-09-21 2017-09-21 Low-density ceramsite proppant and preparation method thereof

Publications (2)

Publication Number Publication Date
CN109536158A true CN109536158A (en) 2019-03-29
CN109536158B CN109536158B (en) 2021-11-26

Family

ID=65828364

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710862659.1A Active CN109536158B (en) 2017-09-21 2017-09-21 Low-density ceramsite proppant and preparation method thereof

Country Status (1)

Country Link
CN (1) CN109536158B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115974525A (en) * 2023-01-12 2023-04-18 重庆聚源塑料股份有限公司 Light ceramsite and preparation method and application thereof

Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1965146A (en) * 2004-06-09 2007-05-16 哈利伯顿能源服务公司 Aqueous-based tackifier fluids and methods of use
CN101247953A (en) * 2005-07-29 2008-08-20 卡博陶粒有限公司 Sintered spherical pellets useful for gas and oil well proppants
CN101560381A (en) * 2009-05-15 2009-10-21 阳泉市长青石油压裂支撑剂有限公司 Ceramic proppant and preparation method thereof
CN101627101A (en) * 2007-04-20 2010-01-13 普拉德研究及开发股份有限公司 Low-density ceramic proppant and its production method
CN101696114A (en) * 2009-10-23 2010-04-21 中钢集团洛阳耐火材料研究院有限公司 Method for preparing light fracturing propping agent for multi-hole oil and gas well
CN102199250A (en) * 2011-03-31 2011-09-28 中国科学院青岛生物能源与过程研究所 Method for preparing anionic polyacrylamide microspheres
CN1985067B (en) * 2004-06-09 2012-02-22 哈利伯顿能源服务公司 Methods of controlling particulates, method for coating partial surface of underground stratum and fluid for controlling clastic particles
CN104364343A (en) * 2012-04-19 2015-02-18 自悬浮支撑有限公司 Self-suspending proppants for hydraulic fracturing
CN104531124A (en) * 2014-12-09 2015-04-22 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 Temperature-control-degradable crack diverting agent prepared by coating precrosslinked gel coated on haydite
CN104946235A (en) * 2014-03-28 2015-09-30 北京仁创科技集团有限公司 Preparation method of self-suspension proppant and prepared proppant
CN104948159A (en) * 2014-03-28 2015-09-30 北京仁创科技集团有限公司 Natural water fracturing construction method
CN105705609A (en) * 2013-11-15 2016-06-22 陶氏环球技术有限责任公司 Proppants with improved dust control
CN105754580A (en) * 2016-03-25 2016-07-13 山东诺尔生物科技有限公司 Preparation method of low-friction self-suspending proppant for fracturing
CN105906318A (en) * 2016-04-22 2016-08-31 太原科技大学 Low-density ceramsite proppant prepared from utilization, and preparation method thereof
CN106336242A (en) * 2016-08-25 2017-01-18 邯郸市马头盛火陶瓷有限公司 Ultra-lightweight porous ceramsite supporting agent and preparation method thereof
CN106634939A (en) * 2016-11-30 2017-05-10 王展旭 Preparation method for self-suspension propping agent in laboratory
CN107033870A (en) * 2017-04-21 2017-08-11 常州市奥普泰科光电有限公司 A kind of preparation method of low-density and high-strength petroleum fracturing propping agent
CN107033871A (en) * 2017-06-08 2017-08-11 广汉华星新技术开发研究所(普通合伙) It is a kind of from suspended prop and preparation method thereof

Patent Citations (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1965146A (en) * 2004-06-09 2007-05-16 哈利伯顿能源服务公司 Aqueous-based tackifier fluids and methods of use
CN1985067B (en) * 2004-06-09 2012-02-22 哈利伯顿能源服务公司 Methods of controlling particulates, method for coating partial surface of underground stratum and fluid for controlling clastic particles
CN101247953A (en) * 2005-07-29 2008-08-20 卡博陶粒有限公司 Sintered spherical pellets useful for gas and oil well proppants
CN101627101A (en) * 2007-04-20 2010-01-13 普拉德研究及开发股份有限公司 Low-density ceramic proppant and its production method
CN101560381A (en) * 2009-05-15 2009-10-21 阳泉市长青石油压裂支撑剂有限公司 Ceramic proppant and preparation method thereof
CN101696114A (en) * 2009-10-23 2010-04-21 中钢集团洛阳耐火材料研究院有限公司 Method for preparing light fracturing propping agent for multi-hole oil and gas well
CN102199250A (en) * 2011-03-31 2011-09-28 中国科学院青岛生物能源与过程研究所 Method for preparing anionic polyacrylamide microspheres
CN104379697A (en) * 2012-04-19 2015-02-25 自悬浮支撑有限公司 Self-suspending proppants for hydraulic fracturing
CN104364343A (en) * 2012-04-19 2015-02-18 自悬浮支撑有限公司 Self-suspending proppants for hydraulic fracturing
CN105705609A (en) * 2013-11-15 2016-06-22 陶氏环球技术有限责任公司 Proppants with improved dust control
CN104946235A (en) * 2014-03-28 2015-09-30 北京仁创科技集团有限公司 Preparation method of self-suspension proppant and prepared proppant
CN104948159A (en) * 2014-03-28 2015-09-30 北京仁创科技集团有限公司 Natural water fracturing construction method
CN104531124A (en) * 2014-12-09 2015-04-22 中国石油集团川庆钻探工程有限公司长庆井下技术作业公司 Temperature-control-degradable crack diverting agent prepared by coating precrosslinked gel coated on haydite
CN105754580A (en) * 2016-03-25 2016-07-13 山东诺尔生物科技有限公司 Preparation method of low-friction self-suspending proppant for fracturing
CN105906318A (en) * 2016-04-22 2016-08-31 太原科技大学 Low-density ceramsite proppant prepared from utilization, and preparation method thereof
CN106336242A (en) * 2016-08-25 2017-01-18 邯郸市马头盛火陶瓷有限公司 Ultra-lightweight porous ceramsite supporting agent and preparation method thereof
CN106634939A (en) * 2016-11-30 2017-05-10 王展旭 Preparation method for self-suspension propping agent in laboratory
CN107033870A (en) * 2017-04-21 2017-08-11 常州市奥普泰科光电有限公司 A kind of preparation method of low-density and high-strength petroleum fracturing propping agent
CN107033871A (en) * 2017-06-08 2017-08-11 广汉华星新技术开发研究所(普通合伙) It is a kind of from suspended prop and preparation method thereof

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
孟昆等: "反相乳液聚合法制备聚丙烯酰胺 ", 《石油化工》 *
张忠兴等: "反相悬浮共聚合成聚丙烯酰胺的中试研究 ", 《北京化工大学学报》 *
王雨华,刘景凤: "高分子量阴离子型聚丙烯酰胺的制备 ", 《石油化工高等学校学报(自然科学版)》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115974525A (en) * 2023-01-12 2023-04-18 重庆聚源塑料股份有限公司 Light ceramsite and preparation method and application thereof
CN115974525B (en) * 2023-01-12 2023-10-27 重庆聚源塑料股份有限公司 Light ceramsite and preparation method and application thereof

Also Published As

Publication number Publication date
CN109536158B (en) 2021-11-26

Similar Documents

Publication Publication Date Title
US10822921B2 (en) Methods of using superabsorbent polymers for fracturing and sand control applications
CN103275694B (en) A kind of Clean-water-carryingpetroleum petroleum proppant for petroleum production of low-permeability petroleum reservoir and preparation method thereof
CN104244998B (en) Freeze thawing resistance for cement composition damages the adulterating agent and method that are damaged with anti-strip
CN101696114B (en) Method for preparing light fracturing propping agent for multi-hole oil and gas well
CN108084989B (en) Effervescent gas suspension proppant for slickwater fracturing and preparation method thereof
CN103131406A (en) Super-hydrophobic propping agent and preparation method
CN109777387B (en) Repeated fracturing temporary plugging agent and preparation method and application thereof
CN106832145A (en) A kind of gas suspension proppant for slippery water pressure break and preparation method thereof and application method
CN104861110B (en) Thief zone heavy crude reservoir is prevented swollen pressing down sand agent and preparation method thereof
CN106398669B (en) A kind of preparation method of drilling fluid pressurization sealing agent
CN111548779B (en) Temporary plugging agent and preparation method thereof
CN104530294A (en) High-strength silicon dioxide and clay dual nano-composite hydrogel and preparation method thereof
CN107815300B (en) Oil-containing sludge profile control plugging agent and preparation method thereof
WO2011081550A1 (en) Hydraulic fracturing system
CN109385263A (en) A kind of low-density film-coated ceramisite proppant and preparation method thereof
CN104152135B (en) One oil field low-density and high-strength riverfrac treatment proppant and preparation method
CN106517804A (en) Hollow glass beads and application thereof
CN109536158A (en) A kind of low-density ceramic proppant and preparation method thereof
CN106190093A (en) Ceramsite propping agent used in coal bed gas hydraulic fracture mining and preparation method thereof
CN114592846A (en) Coal seam fracturing and multi-effect enhanced extraction method based on gas-liquid two-phase carbon dioxide
CN105131934A (en) Double-layer high-strength fracturing propping agent and preparing method thereof
CN110846008A (en) Oil well cement lightening admixture
CN106866243A (en) A kind of method that utilization sludge prepares ceramsite propping agent and composite fertilizer
CN106367058A (en) Low-density waterproof lamination propping agent and preparation method
CN106433602B (en) A kind of cleaning foam fracturing fluid thickening agent and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant