CN1386769A - Amphoteric ion polymer and its preparing process and use - Google Patents
Amphoteric ion polymer and its preparing process and use Download PDFInfo
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- CN1386769A CN1386769A CN 02104242 CN02104242A CN1386769A CN 1386769 A CN1386769 A CN 1386769A CN 02104242 CN02104242 CN 02104242 CN 02104242 A CN02104242 A CN 02104242A CN 1386769 A CN1386769 A CN 1386769A
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Abstract
The amphoteric ion polymers including viscosity increaser, impervious agent and detackifier for well-drilling fluid is prepared from 3 cationic monomers, 2 anionic monomers and 2 non-ionic monomers through proportional mixing, and instantaneous polymerization by evaporating to desolventize. Their molecular weights are controlled. Its advantages are a certain power for resisting high temp and pollution, and better rheological property and wall-forming performance.
Description
FIELD OF THE INVENTION
The present invention relates to drilling well with amphoteric ion polymer and preparation method and purposes, more particularly, the present invention relates to be applicable to new type amphoteric ionic polymer and preparation method petroleum drilling and completion engineering, that be used as tackifier, fluid loss agent and viscosity-depression agent.
Technical background
The major function of drilling fluid in drilling engineering is the bottom-hole cleaning, the suspension cutting carring; Form mud cake, the protection borehole wall; Control and equilibrium strata pressure; The heat that cooling produces because of high-pressure jet drilling; Lubricated drill bit and drill string; Improve drilling speed etc.One of problem of greatest concern is a stabilizing borehole in the drilling fluid engineering, especially to water sensitivity mud shale, high-pressure jet drilling in addition.Prevent that shale from collapsing, suppressing the aquation dispersion to greatest extent is that oilfield chemistry is studied unremitting problem always.The appearance of polymer mud makes inhibition shale aquation disperse to be improved.But the acquisition of negatively charged ion or non-ionic polyalcohol mud inhibition is mainly by following three aspects: increase polymericular weight as far as possible; Composite use inorganic salt; Increase adsorption group ratio on the polymer molecular chain.Though above measure has the effect of certain enhancing mud inhibition, but when improving the mud inhibition, strengthened the flocculation trend of mud suspension system medium clay soil, the viscosity of drilling fluid, shear force rise very fast, destroyed the stability of mud system, totally unfavorable to high-pressure jet drilling.The enhancing of past mud inhibition is a cost to sacrifice the mud superperformance all the time.
For adapting to the needs of high-pressure jet drilling, require drilling fluid to realize not disperseing and low solid phase.Do not disperse meaning that drilling cuttings is had strong inhibition aquation dispersive ability, low solid phase meaning water-base drilling fluid hangs down solid phase as much as possible and adopts effective polymkeric substance, the protection wellbore stability.Developed amphoteric ion polymer (CN1149070A the nineties in last century, on May 7th, 1997 is open) adapted to the demand, its significant technical characterictic is: the existence of cation group makes the interaction mode of polymer molecular chain and clay particle surface become adsorption by hydrogen bond by adsorption by hydrogen bond and coordinate bond absorption, coordinate bond absorption exists simultaneously with chemical bond, adsorption strength and the rate of adsorption of polymer molecular chain on clay significantly improved, so amphoteric ion polymer can be before the drilling cuttings aquation be disperseed, in time securely it is wrapped by also anhydrating of appropriateness and appropriateness are protected glue in the mode of chain bundle or chain group, when realizing the polymkeric substance strong rejection capability, also guarantee rheological and building capacity that drilling fluid is good, help high-pressure jet drilling and improve drilling speed.
But above-mentioned amphoteric ion polymer still can not satisfy the requirement of drilling operation in some aspects, and for example the viscosity of drilling fluid tackifier is still waiting to improve, and also needs further to increase the mud mud yield and strengthens filtration reduction.
The inventor is through research with keen determination, developed a kind of new type amphoteric ionic polymer, amphoteric ion polymer of the present invention is owing to introduce the cationic monomer that contains the diene key, when its consumption surpasses 5.0% (accounting for the weight percent of monomer total amount), make polymkeric substance have little crosslinked feature.Little crosslinked viscosity that can effectively improve drilling fluid tackifier, and increase the mud mud yield and strengthen filtration reduction, further improve the efficient of drilling operation, thereby finished the present invention.
The content of invention
The purpose of this invention is to provide a kind of novel amphoteric ion polymer and preparation method and as the purposes of tackifier, fluid loss agent and viscosity-depression agent.
Amphoteric ion polymer of the present invention is the cross-linking copolymer of one or more positively charged ions, negatively charged ion and non-ionic monomer, and wherein positively charged ion, negatively charged ion and non-ionic monomer are respectively: 1. cationic monomer:
In the formula:
R
1, R
4: C
1～C
6Alkyl or benzyl
R
2, R
3: H or C
1～C
3Alkyl
A: F, Cl, Br, I, BF
4Or PF
6
P: 1～3 positive integer 2. anionic monomers:
II-1：????????CH
2＝CH-R
5
In the formula:
R
5: COOH, COOM or (CH
2)
rSO
3M
(M is H, basic metal, alkaline-earth metal or ammonium; R is 1～16 positive integer) and/or
In the formula:
R
6, R
7, R
8: H or C
1～C
12Alkyl
M:H, basic metal, alkaline-earth metal or ammonium
In the formula:
R
9, R
10: H or C
1～C
3Alkyl, and/or
In the formula: R
11: C ≡ N or benzyl
R
12: H or CH
3
In the tackifier of amphoteric ion polymer of the present invention, fluid loss agent and the viscosity-depression agent, all kinds of monomeric weight percents are different, and concrete numerical value sees Table 1:
Table 1: the monomer content of the different agent kinds of polymkeric substance compares *
* each monomer weight percentage ratio is combined into 100%
| Monomeric species | Tackifier % | Fluid loss agent % | Viscosity-depression agent % |
| Cationic monomer I-1 or I-3 | ????5～40 | ????5～40 | ????5～20 |
| Cationic monomer I-2 | ????5～20 | ????5～20 | ????0～5 |
| Anionic monomer II-1 | ????5～60 | ????5～50 | ????5～90 |
| Anionic monomer II-2 | ????5～50 | ????5～50 | ????5～50 |
| Non-ionic monomer III-1 | ????5～90 | ????5～60 | ????0～20 |
| Non-ionic monomer III-2 | ????5～20 | ????5～20 | ?????0～20 |
The viscosity-average molecular weight of the tackifier of amphoteric ion polymer of the present invention, fluid loss agent and viscosity-depression agent (molecular weight system is converted into the polyacrylamide viscosity-average molecular weight, hereinafter to be referred as molecular weight) should meet following requirement respectively:
The molecular weight of tackifier: 1 * 10
6～8 * 10
6
The molecular weight of fluid loss agent: 5 * 10
4～1 * 10
6
The molecular weight of viscosity-depression agent: 0.3～5 * 10
4
In the polymerization process of the present invention, to the molecular weight employing conditioning agent control of low-molecular weight polymer.Conditioning agent is alkyl sulfhydryl such as ethanethio, and Thiovanic acid, mercaptoethanol, mercaptoamino-acid, mercapto ethyl iminodiethanoic acid or their mixture also can cooperate copper sulfate to use.The consumption of molecular weight regulator accounts for 0～10% of total monomer weight.
Polymerization initiation of the present invention is a redox initiation system, as persulphate and hydrosulphite, sulphite and the thiosulphate of basic metal or ammonium.Initiator amount accounts for 0.01%～10% of total monomer weight.
Polymerization process of the present invention adopts vaporization desolventizing instaneous polymerization method.Polymerisation medium is a water, and monomeric effective weight percentage concentration (referring to that whole monomers account for the concentration expressed in percentage by weight of polymer fluid gross weight as solute) is 50%～90%.With redox system normal temperature initiated polymerization, the polymerization deadline is 1～10 minute, and polymerisate is porous elasticity semisolid or solid (moisture 5%～25%).
The polymer monomer that uses among the present invention and other raw material can have been bought or prepare according to ordinary method from the market.
Amphoteric ion polymer of the present invention at home and abroad is widely used in the oil field.
Embodiment
The present invention describes in detail with following embodiment, but the present invention is not subjected to the restriction of these embodiment.
Embodiment 1 (FA367 1.)
In an open containers, under normal temperature condition, add 40.0 gram water, 50.0 gram acrylamides, 7.5 gram potassium acrylates, 10.0 gram vinyl sulfonic acid sodium, 18.0 gram N successively, N-diethyl diallyl ammonium chloride and 10.0 gram 2-acrylamido-2-methyl propane sulfonic acid sodium stir.Add 5.0 milliliters of (5% concentration of aqueous solution) persulfate aqueous solutions and 2.5 milliliters of (5% concentration of aqueous solution) aqueous solution of sodium bisulfite then.The system temperature of reaction rises to rapidly about 120 ℃ in short period of time, and reactant is the vesicular Hookean body, and moisture 10%～20%.Product is pulverized after drying under 100～110 ℃ of conditions.This product is done the tackifier of drilling fluid and well finishing liquid, and its pH value of water solution equals 7, and molecular weight is 2.47 * 10
6
Embodiment 2 (FA367 2.)
In an open containers, under normal temperature condition, add 60.0 gram water, 50.0 gram acrylamides, 7.5 gram potassium acrylates, 7.5 gram vinyl sulfonic acid sodium, 15.0 gram N while stirring successively, N-diethyl diallyl ammonium chloride and 10.0 gram 2-acrylamido-2-methyl propane sulfonic acid sodium stir.Add 5.0 milliliters of (5% concentration of aqueous solution) persulfate aqueous solutions and 2.5 milliliters of (5% concentration of aqueous solution) aqueous solution of sodium bisulfite then.The system temperature of reaction rises to rapidly about 120 ℃ in short period of time, and reactant is the vesicular Hookean body, and moisture 10%～20%.Product is pulverized after drying under 100～110 ℃ of conditions.This product is done the tackifier of drilling fluid and well finishing liquid, and its pH value of water solution equals 7, molecular weight 3.01 * 10
6
Embodiment 3 (JT888 1.)
In the blender of stirring is housed, add 50.0 gram water, 50.0 gram acrylamides, 30.0 gram sodium acrylates, 10.0 gram vinyl cyanide, 10.0 gram vinyl sulfonic acid sodium, 10.0 gram N successively, N-diethyl diallyl ammonium chloride, 10.0 gram acrylamido oxypropyl trimethyl ammonium chlorides mix the back and add 5.0 milliliters of (10% concentration of aqueous solution) persulfate aqueous solutions and 5.0 milliliters of (10% concentration of aqueous solution) aqueous solution of sodium bisulfite.The system temperature of reaction rises to rapidly about 120 ℃ in short period of time, and reactant is the vesicular Hookean body, and moisture 10%～20%.Product is pulverized after drying under 100～110 ℃ of conditions.This product is cooked the fluid loss agent of drilling fluid and well finishing liquid, and its pH value of water solution equals 7, and molecular weight is 0.87 * 10
6
Embodiment 4 (JT888 2.)
In the blender of stirring is housed, add 40.0 gram water, 50.0 gram acrylamides, 40.0 gram potassium acrylates, 10.0 gram vinyl cyanide, 10.0 gram sodium allylsulfonates, 10.0 gram N successively, N-diethyl diallyl ammonium chloride, 10.0 gram N, N, N-trimethylammonium allyl ammonium chloride, 10.0 gram 2-acrylamido-2-methyl propane sulfonic acid sodium mix the back and add 5.0 milliliters of (10% concentration of aqueous solution) persulfate aqueous solutions and 5.0 milliliters of (10% concentration of aqueous solution) aqueous solution of sodium bisulfite.The system temperature of reaction rises to rapidly about 120 ℃ in short period of time, and reactant is the vesicular Hookean body, and moisture 10%～20%.Product is pulverized after drying under 100～110 ℃ of conditions.This product is cooked the fluid loss agent of drilling fluid and well finishing liquid, and its pH value of water solution equals 7, and molecular weight is 0.71 * 10
6
Embodiment 5 (XY27 1.)
In the blender of stirring is housed, add 40.0 gram water successively, 10.0 gram acrylamide, 80.0 gram potassium acrylate, 30.0 gram vinyl sulfonic acid sodium, 5.0 gram N, N-diethyl diallyl ammonium chloride, 10.0 gram N, N-diethyl-N-benzyl allyl ammonium chloride and 5.0 gram alkyl sulfhydryls, mix the back and add 7.5 milliliters of (20% concentration of aqueous solution) ammonium persulfate aqueous solutions and 7.5 milliliters of (20% concentration of aqueous solution) sodium thiosulfate solutions, the short period of time interior reaction temperature rises to rapidly about 120 ℃, heat of polymerization evaporates large quantity of moisture, reaction product is the vesicular solid, under normal temperature condition, dry, pulverize again.This product is cooked the viscosity-depression agent of drilling fluid and well finishing liquid, and its pH value of water solution equals 5.5～7, and molecular weight is 1.03 * 10
4
Embodiment 6 (XY27 2.)
In the blender of stirring is housed, add 40.0 gram water successively, 10.0 gram acrylamide, 90.0 gram potassium acrylate, 20.0 gram sodium allylsulfonate, 10.0 gram acrylamido oxypropyl trimethyl ammonium chloride, 10.0 gram N, N-diethyl-N-benzyl allyl ammonium chloride and 3.0 gram Thiovanic acids and 1.0 gram mercapto ethyl iminodiethanoic acids, mix the back and add 7.5 milliliters of (20% concentration of aqueous solution) ammonium persulfate aqueous solutions and 7.5 milliliters of (20% concentration of aqueous solution) aqueous solution of sodium bisulfite, the short period of time interior reaction temperature rises to rapidly about 120 ℃, heat of polymerization evaporates large quantity of moisture, reaction product is the vesicular solid, under normal temperature condition, dry, pulverize again.This product is cooked the viscosity-depression agent of drilling fluid and well finishing liquid, and its pH value of water solution equals 5.5～7, and molecular weight is 0.69 * 10
4
Embodiment 7
Amphoteric ion polymer tackifier of the present invention, fluid loss agent and viscosity-depression agent, estimate (following slurry test with) by the corresponding test method of " API drilling fluid class standard ", rheological (apparent viscosity AV, plastic viscosity PV, yield value YP and the ratio of dynamic shear force/yield value to plastic viscosity YP/PV of test mud after normal temperature and 120 ℃ of heat are rolled aging (16 hours).) and filter loss.In addition, the tackifier B-1 among new type amphoteric ionic polymer tackifier of the present invention, fluid loss agent and viscosity-depression agent and the CN 1149070, fluid loss agent B-2 performance are compared, auspiciously see Table 1, table 2 and table 3.
The slurry of joining of table 1 amphoteric ion polymer tackifier is tested
| Prescription | PH value | ??AV (MPa.s) | ??PV (MPa.s) | ??YP ??(Pa) | ?YP/PV | Filter loss (ml) | Remarks |
| 4% fresh water base slurry | ??10.0 | ??8.5 | ??3.0 | ??5.5 | ??1.83 | ??27.0 | Normal temperature |
| 4% fresh water base slurry+0.1%FA367 1. | ??9.0 | ??23.0 | ??12.0 | ??11.0 | ??0.91 | ??13.9 | |
| 4% fresh water base slurry+0.3%FA367 1. | ??9.0 | ??39.0 | ??22.5 | ??16.5 | ??0.73 | ??12.4 | |
| 4% fresh water base slurry+0.1%B-1 | ??9.0 | ??19.0 | ??9.0 | ??7.0 | ??0.78 | ??16.2 | |
| 4% fresh water base slurry+0.3%B-1 | ??9.0 | ??30.5 | ??16.0 | ??10.0 | ??0.63 | ??13.9 |
| 4% fresh water base slurry | ??9.5 | ??8.5 | ????5.0 | ????3.5 | ????0.70 | ??30.0 | 120 ℃ of heat are rolled 16h |
| 4% fresh water base slurry+0.1%FA367 1. | ??9.0 | ??9.3 | ????7.0 | ????2.3 | ????0.33 | ??15.5 | |
| 4% fresh water base slurry+0.3%FA367 1. | ??9.0 | ??18.3 | ????12.5 | ????5.8 | ????0.46 | ??12.5 | |
| 4% fresh water base slurry+0.1%B-1 | ??9.0 | ??8.8 | ????5.5 | ????4.0 | ????0.73 | ??25.0 | |
| 4% fresh water base slurry+0.3%B-1 | ??9.0 | ??13.3 | ????9.7 | ????4.5 | ????0.46 | ??19.9 |
The slurry of joining of table 2 amphoteric ion polymer fluid loss additive is tested
| Prescription | PH value | ????AV ??(MPa.s) | ????PV ??(MPa.s) | ??YP ??(Pa) | ??YP/PV | Filter loss (ml) | Remarks |
| 4% fresh water base slurry | ??9.5 | ????7.5 | ????3.0 | ??4.8 | ??1.60 | ??28.5 | Normal temperature |
| 4% fresh water base slurry+0.2%JT888 1. | ??9.0 | ????12.0 | ????7.5 | ??4.5 | ??0.60 | ??14.5 | |
| 4% fresh water base slurry+0.5%JT888 1. | ??9.0 | ????17.0 | ????11.0 | ??6.0 | ??0.54 | ??10.5 | |
| 4% fresh water base slurry+0.2%B-2 | ??9.0 | ????11.5 | ????6.5 | ??4.5 | ??0.69 | ??21.3 | |
| 4% fresh water base slurry+0.5%B-2 | ??9.0 | ????15.0 | ????10.5 | ??6.5 | ??0.62 | ??15.8 | |
| 4% fresh water base slurry | ??9.5 | ????8.5 | ????5.0 | ??3.5 | ??0.70 | ??32.0 | 120 ℃ of heat are rolled 16h |
| 4% fresh water base slurry+0.2%JT888 1. | ??9.0 | ????5.0 | ????3.5 | ??1.5 | ??0.43 | ??17.8 | |
| 4% fresh water base slurry+0.5%JT888 1. | ??9.0 | ????8.8 | ????6.0 | ??2.8 | ??0.47 | ??14.5 | |
| 4% fresh water base slurry+0.2%B-2 | ??9.0 | ????5.0 | ????3.0 | ??1.5 | ??0.50 | ??24.1 | |
| 4% fresh water base slurry+0.5%B-2 | ??9.0 | ????8.5 | ????5.5 | ??3.0 | ??0.55 | ??19.6 |
The slurry of joining of table 3 amphoteric ion polymer viscosity-depression agent is tested
[*] high temperature test is that 160 ℃ of heat are rolled test data after 16 hours.
| Prescription | XY27 is dosage % 1. | PH value | Cold test | High temperature test * | |||
| ????Φ600 | ??Φ100 | Viscosity break ratio % | Φ600 | Viscosity break ratio % | |||
| 4% fresh water base slurry+0.5%FA367 1. | ?0.00 ?0.10 ?0.20 ?0.30 | ?9.0 ?9.0 ?9.0 ?9.0 | ????105.0 ????36.0 ????26.0 ????23.0 | ??58.0 ??20.0 ??14.5 ??12.0 | ??/ ??65.5 ??75.0 ??79.3 | ???/ ???/ ???/ ???/ | ????/ ????/ ????/ ????/ |
| 7% fresh water base slurry+0.1%FA367 1. | ?0.00 ?0.10 ?0.20 ?0.30 | ?9.0 ?9.0 ?9.0 ?9.0 | ????145.0 ????29.0 ????21.8 ????11.6 | ??95.0 ??19.0 ??14.3 ??7.5 | ??/ ??80.0 ??85.0 ??92.1 | ????/ ????/ ????/ ????/ | ??/ ??/ ??/ ??/ |
| 10% fresh water base slurry | ?0.00 ?0.10 ?0.20 ?0.30 | ?9.0 ?9.0 ?9.0 ?9.0 | ????105.0 ????25.0 ????15.0 ????11.0 | ??90.0 ??20.0 ??15.0 ??10.0 | ??0.00 ??77.8 ??83.3 ??88.9 | ????120.0 ????62.0 ????51.5 ????40.0 | ??/ ??48.3 ??57.1 ??66.7 |
Embodiment 8
Amphoteric ion polymer of the present invention has certain temperature resistance contamination resistance, tests it at salt water (4.5%NaCl, 1.3%MgCl
2, 0.5%CaCl
2) mud, saturated brine (35%NaCl) mud and contain 1.5%CaCl
2In normal temperature and 120 ℃ of anti-aging tests, and compare in the mud with tackifier B-1, fluid loss agent B-2 performance among the CN 1149070.Test-results sees Table 4 and table 5.
The normal temperature antipollution test of table 4 amphoteric ion polymer
Table 5: 120 ℃ of anti-aging antipollution tests of amphoteric ion polymer
Embodiment 9
| Drilling fluid composition | The pH value | ????AV ??(mPa.S) | ????PV ??(mPa.S) | ????YP ????(Pa) | ???YP/PV | Filter loss (ml) |
| Salt water base slurry | ?7.0 | ????5.5 | ????3.5 | ????2.8 | ????0.80 | ????72.0 |
| Salt water base slurry+1.2%FA367 1. | ?7.0 | ????31.5 | ????26.5 | ????8.0 | ????0.30 | ????5.0 |
| Salt water base slurry+1.5%JT888 1. | ?7.0 | ????5.3 | ????4.0 | ????1.5 | ????0.38 | ????12.0 |
| Salt water base slurry+1.2%B-1 | ?7.0 | ????25.5 | ????20.0 | ????7.0 | ????0.35 | ????9.3 |
| Salt water base slurry+1.5%B-2 | ?7.0 | ????5.5 | ????4.0 | ????1.5 | ????0.38 | ????14.0 |
| The water base slurry of saturated salt | ?7.0 | ????9.0 | ????6.5 | ????2.5 | ????0.38 | ????97.4 |
| Water base slurry+the 1.2%FA367 of saturated salt 1. | ?7.0 | ????24.0 | ????19.0 | ????8.0 | ????0.42 | ????5.8 |
| Water base slurry+the 1.5%JT888 of saturated salt 1. | ?7.0 | ????14.0 | ????11.5 | ????2.5 | ????0.22 | ????13.0 |
| Water base slurry+the 1.2%B-1 of saturated salt | ?7.0 | ????20.5 | ????16.5 | ????6.5 | ????0.39 | ????8.4 |
| Water base slurry+the 1.5%B-2 of saturated salt | ?7.0 | ????13.0 | ????9.5 | ????2.5 | ????0.26 | ????17.8 |
| CaCl 2The base slurry | ?7.0 | ????4.5 | ????2.5 | ????1.5 | ????0.60 | ????85.0 |
| CaCl 2Base slurry+1.2%FA367 1. | ?7.0 | ????15.3 | ????12.0 | ????4.5 | ????0.38 | ????15.1 |
| ?CaCl 2Base slurry+1.5%JT888 1. | ?7.0 | ????8.8 | ????5.0 | ????3.0 | ????0.60 | ????20.0 |
| ?CaCl 2Base slurry+1.2%B-1 | ?7.0 | ????13.0 | ????10.5 | ????3.5 | ????0.33 | ????15.2 |
| ?CaCl 2Base slurry+1.5%B-2 | ?7.0 | ????8.0 | ????5.0 | ????2.5 | ????0.50 | ????22.0 |
| Drilling fluid composition | The pH value | ?????AV ??(mPa.S) | ????PV ??(mPa.S) | ????YP ????(Pa) | ??YP/PV | Filter loss (ml) |
| Salt water base slurry | ?7.0 | ????3.5 | ????2.0 | ????1.5 | ??0.75 | ????91.0 |
| Salt water base slurry+1.2%FA367 1. | ?7.0 | ????6.3 | ????4.5 | ????2.0 | ??0.44 | ????31.0 |
| Salt water base slurry+1.5%JT888 1. | ?7.0 | ????3.5 | ????2.5 | ????1.0 | ??0.40 | ????18.0 |
| Salt water base slurry+1.2%B-1 | ?7.0 | ????5.5 | ????4.5 | ????2.0 | ??0.44 | ????45.8 |
| Salt water base slurry+1.5%B-2 | ?7.0 | ????3.5 | ????2.5 | ????1.0 | ??0.40 | ????35.7 |
| The water base slurry of saturated salt | ?7.0 | ????6.0 | ????4.0 | ????2.0 | ??0.50 | ????99.4 |
| Water base slurry+the 1.2%FA367 of saturated salt 1. | ?7.0 | ????10.8 | ????7.5 | ????2.0 | ??0.27 | ????15.0 |
| Water base slurry+the 1.5%JT888 of saturated salt 1. | ?7.0 | ????6.0 | ????4.5 | ????1.0 | ??0.22 | ????10.2 |
| Water base slurry+the 1.2%B-1 of saturated salt | ?7.0 | ????10.0 | ????7.0 | ????2.0 | ??0.29 | ????30.4 |
| Water base slurry+the 1.5%B-2 of saturated salt | ?7.0 | ????6.0 | ????4.0 | ????1.0 | ??0.25 | ????21.3 |
| CaCl 2The base slurry | ?7.0 | ????5.0 | ????3.0 | ????2.0 | ??0.67 | ????126.0 |
| CaCl 2Base slurry+1.2%FA367 1. | ?7.0 | ????5.0 | ????3.5 | ????2.0 | ??0.57 | ????33.3 |
| CaCl 2Base slurry+1.5%JT888 1. | ?7.0 | ????4.0 | ????2.5 | ????2.0 | ??0.80 | ????20.1 |
| CaCl 2Base slurry+1.2%B-1 | ?7.0 | ????5.0 | ????3.5 | ????2.0 | ??0.57 | ????68.4 |
| CaCl 2Base slurry+1.5%B-2 | ?7.0 | ????3.5 | ????2.5 | ????2.0 | ??0.80 | ????45.5 |
The test (90 ℃ of test temperatures) of the inhibition drilling cuttings aquation dispersive ability of amphoteric ion polymer tackifier of the present invention, fluid loss agent sees Table 6.Table 6 amphoteric ion polymer suppresses the distributed test of drilling cuttings aquation
[* *]-composite treating agent be 0.30% FA367 1., 1. 0.50% JT888 reach 0.20% XY27 mixed processing agent 1..
| Prescription | Agent dosage (%) | PH value | Drilling cuttings reclaims (g) | Cuttings recovery (%) |
| 4% fresh water base slurry+30g drilling cuttings | ??0.00 | ??7.0 | ????3.0 | ????10.0 |
| 4% fresh water base slurry+30g drilling cuttings+FA367 1. | ??0.30 | ??8.0 | ????22.8 | ????76.0 |
| 4% fresh water base slurry+30g drilling cuttings+JT888 1. | ??0.50 | ??8.0 | ??24.0 | ????80.0 |
| 4% fresh water base slurry+30g drilling cuttings+composite treating agent ** | ??1.00 | ??8.0 | ??24.6 | ????82.0 |
The above results shows that amphoteric ion polymer of the present invention has certain temperature resistance contamination resistance, make drilling fluid suppress clay water and divide the ability of loosing enhancing, have good rheological and building capacity at tackify or viscosity reduction or when falling leak-off, help high-pressure jet drilling and improve drilling speed.
Claims (7)
1. amphoteric ion polymer, this polymkeric substance is the cross-linking copolymer of one or more positively charged ions, negatively charged ion and non-ionic monomer, is to adopt the preparation of vaporization desolventizing instaneous polymerization method.
2. according to the amphoteric ion polymer of claim 1, wherein positively charged ion, negatively charged ion and non-ionic monomer are respectively: 1) cationic monomer:
In the formula:
R
1, R
4: C
1～C
6Alkyl or benzyl
R
2, R
3: H or C
1～C
3Alkyl
A: F, Cl, Br, I, BF
4Or PF
6
P: 1～3 positive integer 2) anionic monomer: II-1:CH
2=CH-R
5In the formula:
R
5: COOH, COOM or (CH
2)
rSO
3MM is H, basic metal, alkaline-earth metal or ammonium; R be 1～16 positive integer and/or
In the formula:
R
6, R
7, R
8: H or C
1～C
12Alkyl
M:H, basic metal, alkaline-earth metal or ammonium
In the formula:
R
9, R
10: H or C
1～C
3Alkyl and/or
In the formula: R
11: C ≡ N or benzyl
R
12: H or CH
3
3. according to the amphoteric ion polymer of claim 2, wherein the viscosity-average molecular weight of amphoteric ion polymer is 1 * 10
6～8 * 10
6Or 5 * 10
4～1 * 10
6Or 0.3～5 * 10
4
4. the preparation method of the amphoteric ion polymer of claim 1, cationic monomer wherein, anionic monomer and non-ionic monomer are respectively according to claim 1, polymerization process adopts vaporization desolventizing instaneous polymerization method, polymerisation medium is a water, and monomeric effective weight percentage concentration is 50%～90%, with redox system normal temperature initiated polymerization, the polymerization deadline is 1～10 minute, and polymerisate is moisture 5%～25% porous elasticity semisolid or solid.
5. according to the preparation method of claim 4, wherein the molecular weight to low-molecular weight polymer adopts conditioning agent control, the consumption of molecular weight regulator accounts for 0～10% of total monomer weight, and polymerization initiation is a redox initiation system, and initiator amount accounts for 0.01%～10% of total monomer weight.
6. the amphoteric ion polymer of claim 1 is as the purposes of the tackifier in drilling fluid or the well finishing liquid or fluid loss agent or viscosity-depression agent.
7. according to the purposes of claim 7, wherein the viscosity-average molecular weight as the amphoteric ion polymer of tackifier is 1 * 10
6～8 * 10
6Viscosity-average molecular weight as the amphoteric ion polymer of fluid loss agent is 5 * 10
4～1 * 10
6Viscosity-average molecular weight as the amphoteric ion polymer of viscosity-depression agent is 0.3～5 * 10
4
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| CNB02104242XA CN1179990C (en) | 2002-02-25 | 2002-02-25 | Amphoteric ion polymer and its preparing process and use |
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| CNB02104242XA CN1179990C (en) | 2002-02-25 | 2002-02-25 | Amphoteric ion polymer and its preparing process and use |
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| CN1179990C CN1179990C (en) | 2004-12-15 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101691485B (en) * | 2009-07-29 | 2012-03-28 | 西南石油大学 | High temperature resistant amphoteric ion polymer fluid loss agent used for drilling fluid and preparation method thereof |
| CN102433108A (en) * | 2010-09-29 | 2012-05-02 | 中国石油化工股份有限公司 | Temperature-resistance salt-resistance filtrate reducer for drilling fluid and preparation method thereof |
| WO2012083492A1 (en) * | 2010-12-21 | 2012-06-28 | General Electric Company | Methods of cationic polymer detection |
| CN107880213A (en) * | 2017-11-21 | 2018-04-06 | 山东大学 | Super super-heavy crude viscosity-reducing agent of amphipathic polymer that a kind of siloxane quaternary ammonium is modified and preparation method and application |
| CN108641686A (en) * | 2018-05-25 | 2018-10-12 | 成都理工大学 | Superhigh temperature ultrahigh-density water-base drilling fluid completion fluid polycarboxylate flow pattern regulator and preparation method thereof |
| CN115772243A (en) * | 2021-09-06 | 2023-03-10 | 中国石油化工股份有限公司 | Tackifier for solid-free drilling fluid and preparation method and application thereof |
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2002
- 2002-02-25 CN CNB02104242XA patent/CN1179990C/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101691485B (en) * | 2009-07-29 | 2012-03-28 | 西南石油大学 | High temperature resistant amphoteric ion polymer fluid loss agent used for drilling fluid and preparation method thereof |
| CN102433108A (en) * | 2010-09-29 | 2012-05-02 | 中国石油化工股份有限公司 | Temperature-resistance salt-resistance filtrate reducer for drilling fluid and preparation method thereof |
| CN102433108B (en) * | 2010-09-29 | 2014-07-02 | 中国石油化工股份有限公司 | Temperature-resistance salt-resistance filtrate reducer for drilling fluid and preparation method thereof |
| WO2012083492A1 (en) * | 2010-12-21 | 2012-06-28 | General Electric Company | Methods of cationic polymer detection |
| CN107880213A (en) * | 2017-11-21 | 2018-04-06 | 山东大学 | Super super-heavy crude viscosity-reducing agent of amphipathic polymer that a kind of siloxane quaternary ammonium is modified and preparation method and application |
| CN108641686A (en) * | 2018-05-25 | 2018-10-12 | 成都理工大学 | Superhigh temperature ultrahigh-density water-base drilling fluid completion fluid polycarboxylate flow pattern regulator and preparation method thereof |
| CN108641686B (en) * | 2018-05-25 | 2021-01-01 | 成都理工大学 | Flow pattern regulator for ultra-high temperature and ultra-high density water-based drilling fluid and completion fluid and preparation method thereof |
| CN115772243A (en) * | 2021-09-06 | 2023-03-10 | 中国石油化工股份有限公司 | Tackifier for solid-free drilling fluid and preparation method and application thereof |
| CN115772243B (en) * | 2021-09-06 | 2024-02-13 | 中国石油化工股份有限公司 | Tackifier for solid-free drilling fluid and preparation method and application thereof |
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| Publication number | Publication date |
|---|---|
| CN1179990C (en) | 2004-12-15 |
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