CN107880863A - One kind is recovered the oil with corrosion-release scale-proof wax-removal agent and preparation method thereof - Google Patents
One kind is recovered the oil with corrosion-release scale-proof wax-removal agent and preparation method thereof Download PDFInfo
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- CN107880863A CN107880863A CN201610876860.0A CN201610876860A CN107880863A CN 107880863 A CN107880863 A CN 107880863A CN 201610876860 A CN201610876860 A CN 201610876860A CN 107880863 A CN107880863 A CN 107880863A
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/52—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
- C09K8/524—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning organic depositions, e.g. paraffins or asphaltenes
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/52—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/54—Compositions for in situ inhibition of corrosion in boreholes or wells
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2208/00—Aspects relating to compositions of drilling or well treatment fluids
- C09K2208/32—Anticorrosion additives
Abstract
The invention discloses a kind of oil recovery corrosion-release scale-proof wax-removal agent.Every 100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent includes:The oleic acid base hydroxyethyl imidazole quinoline of 5 15 parts by weight;The dodecyl benzyl dimethyl ammonium chloride of 15 20 parts by weight;The 1-hydroxy ethylidene-1,1-diphosphonic acid of 0.5 5 parts by weight;The ATMP of 0.5 2 parts by weight;The ethylenediamine tetra-acetic acid of 0.5 5 parts by weight;The TEPA polyoxyethylene polyoxypropylene ether of 15 20 parts by weight;The fluorine carbon surfactant of 0.2 1 parts by weight;The ethylene glycol of 13 parts by weight;Surplus is water.A kind of recover the oil provided by the invention uses corrosion-release scale-proof wax-removal agent, and not only compatibility is good for the medicament, has both met requirement of the oil well to corrosion-mitigation scale-inhibition, meets requirement of the oil well to wax removal viscosity reduction again, and stability is high.
Description
Technical field
The present invention relates to petroleum industry chemicals technical field, more particularly to it is a kind of recover the oil with corrosion-release scale-proof wax-removal agent and
Its preparation method.
Background technology
Oil well anti-corrosion, scale inhibition, wax removal are a generality problems in oilfield process.
With oil field development, there is serious corrosion and scaling in the continuous rising of water content, oil well bar, pipe, pump in oil well
Phenomenon, oil field development system normal operation is had a strong impact on, effectively to have delayed or suppress the corrosion and fouling of oil well, preferably
Method is periodically to add the chemical agent with corrosion-mitigation scale-inhibition effect into oil well to be safeguarded.
In addition, with oil field development, wax deposition phenomenon is there is also in oil well, causes oil pipe paraffin blockage, area of passage reduce, be negative
The problems such as lotus increase, electric current rising, have a strong impact on oil well output, and preferable method is to add the chemistry with wax removal effect
Medicament is safeguarded.
During the present invention is realized, inventor has found that prior art at least has problems with:With corrosion-mitigation scale-inhibition
The chemical agent of effect and the chemical agent compatibility that there is wax removal to act on are poor, are unfavorable for the common performance of two class pharmacy effects,
Very big difficulty is brought to production management.
The content of the invention
The present invention provides a kind of recover the oil and uses corrosion-release scale-proof wax-removal agent and preparation method thereof, for solving to have in the prior art
The chemical agent and there is the problem of chemical agent compatibility difference of wax removal effect that corrosion-mitigation scale-inhibition acts on.Technical scheme is as follows:
In the first aspect of the present invention, the invention discloses a kind of oil recovery corrosion-release scale-proof wax-removal agent, every 100 parts by weight are adopted
Oil corrosion-release scale-proof wax-removal agent includes:
In the preferred embodiment of the present invention, every 100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent includes:
Specifically, every 100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent includes:
Specifically, every 100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent includes:
Specifically, every 100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent includes:
Specifically, every 100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent includes:
In the preferred embodiment of the present invention, the fluorine carbon surfactant is fluorocarbon surfactant FN-
3。
In the second aspect of the present invention, the preparation method the invention discloses a kind of oil recovery with corrosion-release scale-proof wax-removal agent, bag
Include following steps:
First oleic acid base hydroxyethyl imidazole quinoline, dodecyl benzyl dimethyl ammonium chloride, TEPA polyoxypropylene are gathered
Oxygen vinethene is added in reactor, is slowly heated to temperature while stirring no more than 50 DEG C, is well mixed;
Backward reactor in add 1-hydroxy ethylidene-1,1-diphosphonic acid and ethylene glycol while stirring, be well mixed;
Add ATMP and ethylenediamine tetra-acetic acid while stirring into reactor again, be well mixed;
Then add fluorine carbon surfactant while stirring into reactor, stop adding after being well mixed, side stirring
While it is cooled to room temperature;
Water is finally added while stirring, is well mixed, oil recovery corrosion-release scale-proof wax-removal agent is made;
Wherein, recover the oil and used in corrosion-release scale-proof wax-removal agent described in every 100 parts by weight, the oleic acid base hydroxyethyl imidazole quinoline adds
It is 5-15 parts by weight to enter amount;The addition of the dodecyl benzyl dimethyl ammonium chloride is 15-20 parts by weight;The hydroxyl second
The addition for pitching di 2 ethylhexyl phosphonic acid is 0.5-5 parts by weight;The addition of the ATMP is 0.5-2 parts by weight;The second
The addition of ethylenediamine tetraacetic acid (EDTA) is 0.5-5 parts by weight;The addition of the TEPA polyoxyethylene polyoxypropylene ether is 15-
20 parts by weight;The addition of the fluorine carbon surfactant is 0.2-1 parts by weight;The addition of the ethylene glycol is 1-3 weights
Measure part;Surplus is water.
In the preferred embodiment of the present invention, it is described to be slowly heated to 45-50 DEG C while stirring.
In a kind of more preferably embodiment of the present invention, speed that the temperature of the slow heating rises for 3-5 DEG C/
min。
The beneficial effect of technical scheme provided in an embodiment of the present invention is:One kind oil recovery corrosion-mitigation scale-inhibition provided by the invention
Paraffin remover, not only compatibility is good for the medicament, has both met requirement of the oil well to corrosion-mitigation scale-inhibition, meets oil well again to wax removal viscosity reduction
Requirement, and stability is high.
Embodiment
To make technical scheme and advantage clearer, embodiment of the present invention will be made below further detailed
Thin description.
In the first aspect of the present invention, the embodiment provides a kind of oil recovery corrosion-release scale-proof wax-removal agent.Often adopt
The parts by weight oil recovery corrosion-release scale-proof wax-removal agent of oil corrosion-release scale-proof wax-removal agent 100 includes:
Inventor is it was unexpectedly observed that the oil recovery corrosion-release scale-proof wax-removal agent of the present invention, and not only compatibility is good, has good
The effect of corrosion-release scale-proof wax-removal viscosity reduction, and stability is high, and long-term place is not likely to produce precipitation and gone bad.
Above-mentioned chemical agent used in the present invention is industrial goods.Wherein,
Oleic acid base hydroxyethyl imidazole quinoline, amphoteric ionic surfactant is nonpoisonous and tasteless in light-coloured transparent shape, to skin
It is non-stimulated, good water solubility, a kind of absorption film-forming type corrosion inhibiter, for rejection of oil flied effluent processing system and its pipeline corrosion protection,
Available for crude oil and aqueous fuel transfer system, it can also make diluent of drilling liquid.
Dodecyl benzyl dimethyl ammonium chloride, English name:Dodecyl Dimethyl Benzyl ammonium
Chloride, alias 1227, weak yellow liquid, high-efficiency broad spectrum biocide, suitable for alkalescence and nitrogen, ammoniate water process,
Belong to non-chlorinated type biocide.Dodecyl benzyl dimethyl ammonium chloride is a kind of cationic surfactant, and category is non-oxidizable to kill
Microbial inoculum, there is wide spectrum, efficient sterilization algae removal ability, bacterium algae breeding and foundry loam growth in water can be efficiently controlled, and with good
Good sludge stripping effect and certain scattered, osmosis, at the same have it is certain deoil, deodorizing capability and corrosion inhibition.
It is widely used in the recirculating cooling water system of the industries such as oil, chemical industry, electric power, weaving, to control recirculating cooling water system
Middle bacterium algae is grown.
1-hydroxy ethylidene-1,1-diphosphonic acid, English name:1-Hydroxyethylidene-1,1-diphosphonic acid, referred to as
HEDP, faint yellow or colourless liquid, chemical temperatures are good, high temperature resistant, not facile hydrolysis, are a kind of organophosphor acids scale inhibitors
Agent, stable complex compound can be formed with various metals ions such as iron, copper, zinc, the oxide of metal surface can be dissolved.For oil field
The anti-corrosion, scale-inhibiting of flood pattern;
ATMP, English name:Amino Trimethylene Phosphonic Acid, abbreviation ATMP, nothing
Color or slightly yellow transparency liquid, ATMP have good chelating, lower bound suppression and distortion of lattice effect.Scaling salt in water can be prevented
Class forms the formation of incrustation scale, particularly calcium carbonate scale.ATMP chemical property in water is stable, not facile hydrolysis.In water concentration compared with
Gao Shi, there is good corrosion mitigating effect.ATMP has excellent scale effect, less toxic or nontoxic, and heat endurance is good,
The formation of the formation of scaling salt class incrustation scale, particularly calcium carbonate scale in water can be prevented.For rejection of oil flied effluent processing system and contain
Water fuel transfer system, it can also make diluent of drilling liquid;
Ethylenediamine tetra-acetic acid, English name:Ethylenediaminetetraacetic acid, ethylenediaminetetraacetic acid, white are odorless
Tasteless, colorless crystalline powder, insoluble in alcohol and common organic solvents, cold water (cold water speed is slower), hot water can be dissolved in.Often
Softening for boiler water quality.Prevent fouling.
TEPA polyoxyethylene polyoxypropylene ether, thick liquid, as oil extraction in oil field and oil transportation wax-proofing agent;It is applied to
The dehydration of oil field paraffin level crude oil.
A kind of material for the surface tension that fluorocarbon surfactant can significantly decrease solvent with extremely low concentration is referred to as table
Face activating agent.Fluorocarbon surfactant is most important kind in special surfactant, refers to the hydrocarbon of hc-surfactant
Hydrogen atom in chain is completely or partially replaced by fluorine atoms, i.e., fluorocarbon chain instead of hydrocarbon chain, therefore non-in surfactant
Polar group does not only have the performance of hydrophobic property and unique oleophobic.Outstanding feature is the most:Efficiently, stably, i.e., high surface is lived
Property, high thermodynamic and chemical stability.
Ethylene glycol, as surfactant;Colourless transparent liquid.There is gentle sweet fragrance.It is dissolved in water, it is ethanol, ether, low
Carbocyclic aliphatic hydrocarbon.As solvent, spices, medical disinfectant.Diacetone alcohol is obtained by condensation of acetone, then obtained through liquid-phase hydrogenatin.With
In organic synthesis.With used as pesticides stabilizer, bavin machine oil antifreezing agent etc..2- methyl -2,4- pentanediols have permeability, have to inorganic matter
Good dispersibility.In addition to solvent is made, still prevent for dry cleaning agent, automotive brake fluid, printing-ink, pigment dispersing agent, timber
Rotten agent etc..As solvent, spices, medical disinfectant, fabric with penetrating agent, papermaking and leather processing auxiliary agent.
In order that there is more preferable corrosion-release scale-proof wax-removal viscosity reduction to act on for the oil recovery corrosion-release scale-proof wax-removal agent of the present invention, often
100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent include:
It is highly preferred that every 100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent includes:
It is highly preferred that every 100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent includes:
It is highly preferred that every 100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent includes:
It is highly preferred that every 100 parts by weight oil recovery corrosion-release scale-proof wax-removal agent includes:
As a kind of preferred embodiment of the present invention, the fluorine carbon surfactant can be fluorocarbon surfactant
FN-3.Fluorocarbon surfactant FN-3, molecular formula C16H17F17N2O4, can be used as wetting agent, dispersant, foaming agent, bactericide.
Relative to other fluorine carbon surfactants, (50~100ppm) can at very low concentrations by fluorocarbon surfactant FN-3
Aqueous solution surface tension is dropped into very low level (18~20dyn/cm);With high thermodynamics and chemical stability, can be used for
The systems such as high temperature, strong acid, highly basic, Strong oxdiative medium;With fabulous compatibility, various pH value ranges, all kinds of are can be widely used for
Water-based, anhydrous, powder or Radiation-curing system, and can be compatible well with other surfactants in system and component.In Huang
What the Chemical Industry Press of big vast week chief editor published《Chinese surfactant overview》Fluorocarbon surface is lived in page 463 of one book
Property agent FN-3 (industrial goods) has detailed narration.
In the second aspect of the present invention, the preparation the embodiment provides a kind of oil recovery with corrosion-release scale-proof wax-removal agent
Method, comprise the following steps:
First oleic acid base hydroxyethyl imidazole quinoline, dodecyl benzyl dimethyl ammonium chloride, TEPA polyoxypropylene are gathered
Oxygen vinethene is added in reactor, is slowly heated to temperature while stirring no more than 50 DEG C, is well mixed;
Backward reactor in add 1-hydroxy ethylidene-1,1-diphosphonic acid and ethylene glycol while stirring, be well mixed;
Add ATMP and ethylenediamine tetra-acetic acid while stirring into reactor again, be well mixed;
Then add fluorine carbon surfactant while stirring into reactor, stop adding after being well mixed, side stirring
While it is cooled to room temperature;
Water is finally added while stirring, is well mixed, oil recovery corrosion-release scale-proof wax-removal agent is made;
Wherein, recover the oil and used in corrosion-release scale-proof wax-removal agent described in every 100 parts by weight, the oleic acid base hydroxyethyl imidazole quinoline adds
It is 5-15 parts by weight to enter amount;The addition of the dodecyl benzyl dimethyl ammonium chloride is 15-20 parts by weight;The hydroxyl second
The addition for pitching di 2 ethylhexyl phosphonic acid is 0.5-5 parts by weight;The addition of the ATMP is 0.5-2 parts by weight;The second
The addition of ethylenediamine tetraacetic acid (EDTA) is 0.5-5 parts by weight;The addition of the TEPA polyoxyethylene polyoxypropylene ether is 15-
20 parts by weight;The addition of the fluorine carbon surfactant is 0.2-1 parts by weight;The addition of the ethylene glycol is 1-3 weights
Measure part;Surplus is water.
It should be noted that in the art, described room temperature is commonly also referred to normal temperature, it is considered that is 23 DEG C ± 2 DEG C.
A kind of preferred embodiment as oil recovery with the preparation method of corrosion-release scale-proof wax-removal agent is described slow while stirring
It is heated to 45-50 DEG C.The too low dissolving for being unfavorable for above-mentioned chemical agent of heating-up temperature, the too high oil recovery for influenceing to prepare of heating-up temperature
With the property of medicine of corrosion-release scale-proof wax-removal agent.
A kind of more preferably embodiment as oil recovery with the preparation method of corrosion-release scale-proof wax-removal agent, the slow heating
The speed that temperature rises is 3-5 DEG C/min.
Material and facility
Oleic acid base hydroxyethyl imidazole quinoline, Hangzhou Tuo Mu Science and Technology Ltd.s, 250g/ bottles;
Dodecyl benzyl dimethyl ammonium chloride, Jing Zhou Xin Jing chemical industry Co., Ltd, 500ml/ bottles;
1-hydroxy ethylidene-1,1-diphosphonic acid, multiple star dragon water process Co., Ltd of Xinxiang City, 500ml/ bottles;
ATMP, Changzhou Run Yang Chemical Co., Ltd.s, 500ml/ bottles;
Ethylenediamine tetra-acetic acid, Shanghai Yuan Ye bio tech ltd, 250g/ bottles;
TEPA polyoxyethylene polyoxypropylene ether, Nanjing Guo Chen Chemical Co., Ltd.s, 500ml/ bottles;
Fluorocarbon surfactant FN-3, Shanghai Ci Tai Yilong Industry Co., Ltd., 50g/ bottles;
Ethylene glycol, system Qi chemical products Co., Ltd of Zhengzhou City, 50ml/ bottles;
It is industrial goods, it is commercially available.
Normal pressure enamel reaction still, Jiangsu Yang Yang chemical industry equipments Manufacturing Co., Ltd, model 212-DN80.
Embodiment 1:A kind of oil recovery is with the material component weight of anti-corrosion, scale-inhibiting paraffin remover:Oleic acid base hydroxyethyl imidazole quinoline:
10% (2.5kg);Dodecyl benzyl dimethyl ammonium chloride:17% (4.25kg);1-hydroxy ethylidene-1,1-diphosphonic acid:1.5%
(0.375kg);ATMP:1.5% (0.375kg);Ethylenediamine tetra-acetic acid:1% (0.25kg);TEPA gathers
Oxypropylene APEO:19% (4.75kg);Fluorocarbon surfactant FN-3:0.25% (0.0625kg);Ethylene glycol:
2.5% (0.625kg);Water:47.25% (11.8125kg).
Process for preparation is:First, by oleic acid base hydroxyethyl imidazole quinoline, dodecyl benzyl dimethyl ammonium chloride, four ethene
Five three kinds of raw materials of amine polyoxyethylene polyoxypropylene ether are proportionally added into normal pressure enamel reaction still, stir 30 minutes, are slowly warming up to
50 DEG C, 1-hydroxy ethylidene-1,1-diphosphonic acid, ethylene glycol are proportionally added into while stirring, are continued stirring 30 minutes, are then proportionally added into ammonia
The methylenephosphonic acid of base three, ethylenediamine tetra-acetic acid, it is sufficiently stirred 30 minutes, continues to be proportionally added into fluorocarbon surfactant FN-3, no
After disconnected stirring 30 minutes, stop heating.Cool down while stir, be cooled to normal temperature.Water is proportionally added into, it is stirring while adding,
Stirring discharges after 20 minutes, obtains a kind of oil recovery corrosion-release scale-proof wax-removal agent.
Using effect:The oil well 60-8x wax deposition phenomenons in the first oil recovery factory of North China Oilfield Yan Ling work areas are serious, and with slight
Corrosion and scaling, tried out using the present invention in the well, solve the problems, such as the wax deposition corrosion and scaling of oil well.
Before dosing, oil pumper up stroke electric current has built up 52A, and after dosing, oil pumper up stroke electric current gradually decreases to
41.8A, 19.6% is have dropped, show that medicament meets the requirement of the well wax removal viscosity reduction, and positive effect.
With reference to SYT 5273-2000《Oil field extracted water corrosion inhibiter method of evaluating performance》Standard, surveyed using static corrosion
Determine method, take the recovered water of wild goose 60-8x wells, tested using N80 steel standard test piece at 80 DEG C, research corrosion and inhibition effect
Fruit, data such as table 1 is obtained after standing 7 days.
Confirmatory experiment data of the medicament of table 1 to wild goose 60-8x well corrosion inhibitions
As can be seen from the data in the table, to wild goose 60-8x wells, average corrosion rate is reduced to by the 0.0537mm/a before dosing
0.0083mm/a after dosing, corrosion inhibition rate are about 84.6%, illustrate that medicament meets the requirement of the well inhibition.
With reference to SYT 5673-93《Scale inhibitor for oilfield Reliable Evaluating Methods of Their Performance》Standard, the recovered water of wild goose 60-8x wells is taken to carry out
Experiment, fouling and scale inhibition effect are studied, data such as table 2 is obtained in laboratory.
Confirmatory experiment data of the medicament of table 2 to wild goose 60-8x well scale effects
As can be seen from the data in the table, to wild goose 60-8x wells, scale inhibition performance 92.3%, illustrate that medicament meets the well scale inhibition
Requirement.
In summary, a kind of recover the oil that the present embodiment provides uses corrosion-release scale-proof wax-removal agent, has both met 60-8x pairs of oil well wild goose
The requirement of wax removal viscosity reduction, the requirement to corrosion-mitigation scale-inhibition is met again, oil pumper up stroke electric current declines 19.6%, and corrosion inhibition rate reaches
84.6%, scale inhibition performance is up to 92.3%.
Embodiment 2:A kind of oil recovery is with the material component weight of anti-corrosion, scale-inhibiting paraffin remover:Oleic acid base hydroxyethyl imidazole quinoline:
8.5% (4.25kg);Dodecyl benzyl dimethyl ammonium chloride:18% (9kg);1-hydroxy ethylidene-1,1-diphosphonic acid:2.5%
(1.25kg);ATMP:1% (0.5kg);Ethylenediamine tetra-acetic acid:2.5% (1.25kg);TEPA polyoxy
Propylene APEO:15% (7.5kg);Fluorocarbon surfactant FN-3:0.5% (0.25kg);Ethylene glycol:2.5%
(1.25kg);Water:49.5% (24.75kg).
Process for preparation is:First, by oleic acid base hydroxyethyl imidazole quinoline, dodecyl benzyl dimethyl ammonium chloride, four ethene
Five three kinds of raw materials of amine polyoxyethylene polyoxypropylene ether are proportionally added into normal pressure enamel reaction still, stir 30 minutes, are slowly warming up to
45 DEG C, 1-hydroxy ethylidene-1,1-diphosphonic acid, ethylene glycol are proportionally added into while stirring, are continued stirring 30 minutes, are then proportionally added into ammonia
The methylenephosphonic acid of base three, ethylenediamine tetra-acetic acid, it is sufficiently stirred 30 minutes, continues to be proportionally added into fluorocarbon surfactant FN-3, no
After disconnected stirring 30 minutes, stop heating.Cool down while stir, be cooled to normal temperature.Water is proportionally added into, it is stirring while adding,
Stirring discharges after 20 minutes, obtains a kind of oil recovery corrosion-release scale-proof wax-removal agent.
Using effect:The oil well 63-69x corrosion and scaling phenomenons in the first oil recovery factory of North China Oilfield Yan Ling work areas are serious, and companion
There is slight wax deposition, tried out using the present invention in the well, solve the problems, such as the corrosion and scaling wax deposition of oil well.
With reference to SYT 5273-2000《Oil field extracted water corrosion inhibiter method of evaluating performance》Standard, surveyed using static corrosion
Determine method, take the recovered water of wild goose 63-69x wells, tested using N80 steel standard test piece at 80 DEG C, research corrosion and inhibition
Effect, data such as table 3 is obtained after standing 7 days.
Confirmatory experiment data of the medicament of table 3 to wild goose 63-69x well corrosion inhibitions
As can be seen from the data in the table, to wild goose 63-69x wells, average corrosion rate is reduced by the 0.0312mm/a before dosing
0.0040mm/a after to dosing, corrosion inhibition rate are about 87.9%, illustrate that medicament meets the requirement of the well inhibition.
With reference to SYT 5673-93《Scale inhibitor for oilfield Reliable Evaluating Methods of Their Performance》Standard, the recovered water of wild goose 63-69x wells is taken to enter
Row experiment, studies fouling and scale inhibition effect, data such as table 4 is obtained in laboratory.
Confirmatory experiment data of the medicament of table 4 to wild goose 63-69x well scale effects
As can be seen from the data in the table, to wild goose 63-69x wells, scale inhibition performance 94.6%, illustrate that medicament meets the well scale inhibition
Requirement.
Before dosing, oil pumper up stroke electric current has built up 47A, and after dosing, oil pumper up stroke electric current gradually decreases to
39.9A, 15.2% is have dropped, show that medicament meets the requirement of the well wax removal viscosity reduction, and positive effect.
In summary, a kind of recover the oil that the present embodiment provides uses corrosion-release scale-proof wax-removal agent, has both met oil well wild goose 63-69x
Requirement to corrosion-mitigation scale-inhibition, the requirement to wax removal viscosity reduction is met again, corrosion inhibition rate up to 87.9%, up to 94.6% pump by scale inhibition performance
Machine up stroke electric current declines 15.2%.
Embodiment 3
A kind of oil recovery is with the material component weight of anti-corrosion, scale-inhibiting paraffin remover:Oleic acid base hydroxyethyl imidazole quinoline:5%
(1.875kg);Dodecyl benzyl dimethyl ammonium chloride:15% (5.625kg);1-hydroxy ethylidene-1,1-diphosphonic acid:5% (1.875) kg;
ATMP:2% (0.75kg);Ethylenediamine tetra-acetic acid:0.5% (0.1875kg);TEPA polyoxypropylene gathers
Oxygen vinethene:20% (7.5kg);Fluorocarbon surfactant FN-3:1% (0.375kg);Ethylene glycol:3% (1.125kg);Water:
48.5% (18.1875kg).
Process for preparation is:First, by oleic acid base hydroxyethyl imidazole quinoline, dodecyl benzyl dimethyl ammonium chloride, four ethene
Five three kinds of raw materials of amine polyoxyethylene polyoxypropylene ether are proportionally added into normal pressure enamel reaction still, stir 30 minutes, are slowly warming up to
45 DEG C, 1-hydroxy ethylidene-1,1-diphosphonic acid, ethylene glycol are proportionally added into while stirring, are continued stirring 30 minutes, are then proportionally added into ammonia
The methylenephosphonic acid of base three, ethylenediamine tetra-acetic acid, it is sufficiently stirred 30 minutes, continues to be proportionally added into fluorocarbon surfactant FN-3, no
After disconnected stirring 30 minutes, stop heating.Cool down while stir, be cooled to normal temperature.Water is proportionally added into, it is stirring while adding,
Stirring discharges after 20 minutes, obtains a kind of oil recovery corrosion-release scale-proof wax-removal agent.
Using effect:The oil well 60-81x wax deposition phenomenons in the first oil recovery factory of North China Oilfield Yan Ling work areas are serious, and with light
Microcorrosion fouling, tried out using the present invention in the well, solve the problems, such as the wax deposition corrosion and scaling of oil well.
Before dosing, oil pumper up stroke electric current has built up 53A, and after dosing, oil pumper up stroke electric current gradually decreases to
43.2A, 18.5% is have dropped, show that medicament meets the requirement of the well wax removal viscosity reduction, and positive effect.
With reference to SYT 5273-2000《Oil field extracted water corrosion inhibiter method of evaluating performance》Standard, surveyed using static corrosion
Determine method, take the recovered water of wild goose 60-81x wells, tested using N80 steel standard test piece at 80 DEG C, research corrosion and inhibition
Effect, data such as table 5 is obtained after standing 7 days.
Confirmatory experiment data of the medicament of table 5 to wild goose 60-81x well corrosion inhibitions
As can be seen from the data in the table, to wild goose 60-81x wells, average corrosion rate is reduced by the 0.0366mm/a before dosing
0.0066mm/a after to dosing, corrosion inhibition rate are about 81.9%, illustrate that medicament meets the requirement of the well inhibition.
With reference to SYT 5673-93《Scale inhibitor for oilfield Reliable Evaluating Methods of Their Performance》Standard, the recovered water of wild goose 60-81x wells is taken to enter
Row experiment, studies fouling and scale inhibition effect, data such as table 6 is obtained in laboratory.
Confirmatory experiment data of the medicament of table 6 to wild goose 60-81x well scale effects
As can be seen from the data in the table, to wild goose 60-81x wells, scale inhibition performance 93.5%, illustrate that medicament meets the well scale inhibition
Requirement.
In summary, a kind of recover the oil that the present embodiment provides uses corrosion-release scale-proof wax-removal agent, has both met oil well wild goose 60-81x
Requirement to wax removal viscosity reduction, the requirement to corrosion-mitigation scale-inhibition is met again, oil pumper up stroke electric current declines 18.5%, and corrosion inhibition rate reaches
81.9%, scale inhibition performance is up to 93.5%.
Embodiment 4
A kind of oil recovery is with the material component weight of anti-corrosion, scale-inhibiting paraffin remover:Oleic acid base hydroxyethyl imidazole quinoline:15%
(5.625kg);Dodecyl benzyl dimethyl ammonium chloride:20% (7.5kg);1-hydroxy ethylidene-1,1-diphosphonic acid:0.5%
(0.1875kg);ATMP:0.5% (0.1875kg);Ethylenediamine tetra-acetic acid:5% (1.875kg);Four ethene five
Amine polyoxyethylene polyoxypropylene ether:16% (6) kg;Fluorocarbon surfactant FN-3:0.2% (0.075kg);Ethylene glycol:1%
(0.375kg);Water:41.8% (15.675kg).
Process for preparation is:First, by oleic acid base hydroxyethyl imidazole quinoline, dodecyl benzyl dimethyl ammonium chloride, four ethene
Five three kinds of raw materials of amine polyoxyethylene polyoxypropylene ether are proportionally added into normal pressure enamel reaction still, stir 25 minutes, are slowly warming up to
50 DEG C, 1-hydroxy ethylidene-1,1-diphosphonic acid, ethylene glycol are proportionally added into while stirring, are continued stirring 25 minutes, are then proportionally added into ammonia
The methylenephosphonic acid of base three, ethylenediamine tetra-acetic acid, it is sufficiently stirred 25 minutes, continues to be proportionally added into fluorocarbon surfactant FN-3, no
After disconnected stirring 25 minutes, stop heating.Cool down while stir, be cooled to normal temperature.Water is proportionally added into, it is stirring while adding,
Stirring discharges after 20 minutes, obtains a kind of oil recovery corrosion-release scale-proof wax-removal agent.
Using effect:The oil well 63-38x corrosion and scaling phenomenons in the first oil recovery factory of North China Oilfield Yan Ling work areas are serious, and companion
There is slight wax deposition, tried out using the present invention in the well, solve the problems, such as the corrosion and scaling wax deposition of oil well.
With reference to SYT 5273-2000《Oil field extracted water corrosion inhibiter method of evaluating performance》Standard, surveyed using static corrosion
Determine method, take the recovered water of wild goose 63-38x wells, tested using N80 steel standard test piece at 80 DEG C, research corrosion and inhibition
Effect, data such as table 7 is obtained after standing 7 days.
Confirmatory experiment data of the medicament of table 7 to wild goose 63-38x well corrosion inhibitions
As can be seen from the data in the table, to wild goose 63-38x wells, average corrosion rate is reduced by the 0.0220mm/a before dosing
0.0031mm/a after to dosing, corrosion inhibition rate are about 85.7%, illustrate that medicament meets the requirement of the well inhibition.
With reference to SYT 5673-93《Scale inhibitor for oilfield Reliable Evaluating Methods of Their Performance》Standard, the recovered water of wild goose 63-38x wells is taken to enter
Row experiment, studies fouling and scale inhibition effect, data such as table 8 is obtained in laboratory.
Confirmatory experiment data of the medicament of table 8 to wild goose 63-38x well scale effects
As can be seen from the data in the table, to wild goose 63-38x wells, scale inhibition performance 92.0%, illustrate that medicament meets the well scale inhibition
Requirement.
Before dosing, oil pumper up stroke electric current has built up 48A, and after dosing, oil pumper up stroke electric current gradually decreases to
40.3A, 16.1% is have dropped, show that medicament meets the requirement of the well wax removal viscosity reduction, and positive effect.
In summary, a kind of recover the oil that the present embodiment provides uses corrosion-release scale-proof wax-removal agent, has both met oil well wild goose 63-38x
Requirement to corrosion-mitigation scale-inhibition, the requirement to wax removal viscosity reduction is met again, corrosion inhibition rate up to 85.7%, up to 92.0% pump by scale inhibition performance
Machine up stroke electric current declines 16.1%.
The stability test of embodiment 5
Stability is examined or check with corrosion-release scale-proof wax-removal agent with oil recovery prepared by embodiment 2.
Oil recovery corrosion-release scale-proof wax-removal agent prepared by embodiment 2 is in yellow after just preparing, and clear.In room
Temperature, dry, it is shady and cool under conditions of place longer period of time (such as one month) after, solution is still in yellow, and clear.By its
In the first oil recovery factory of North China Oilfield, Yan Ling work areas 63-69x wells are tried out, and corrosion inhibition rate is up to 87.5%, and scale inhibition performance is up to 93.5%, oil pumper
Up stroke electric current declines 15.0%.This is basically identical with the using effect after just preparing, and meets wild goose 63-69x and inhibition is hindered
The requirement of dirty wax removal, illustrate that a kind of stability of oil recovery corrosion-release scale-proof wax-removal agent provided by the invention is good.
Comparative example
Using existing patent document as foundation, a kind of oil recovery of the similar present invention of investigation is steady with the medicament of corrosion-release scale-proof wax-removal agent
It is qualitative.
2- alkyl -1- ethoxy -3- hydroxypropyl imidazoline sodium phosphates:8% (8g);Dodecyl dimethyl Benzylmagnesium chloride
Amine:12% (12g);FC-N01 fluorocarbon surfactants:0.1% (0.1g);Alkylphenol-polyethenoxy (14) ether:5% (5g);First
Aldehyde:4.5% (4.5g);Hexa:10% (10g);Calgon:6% (6g);1-hydroxy ethylidene-1,1-diphosphonic acid:6%
(6g);Water:48.4% (48.4g).
Process for preparation:First, the light ethyl -3- hydroxypropyls imidazoline sodium phosphates of 2- alkyl -1-, dodecyl dimethyl benzyl
Ammonium chloride, FC-N01 fluorocarbon surfactants, alkylphenol-polyethenoxy (14) ether, formaldehyde, hexa, hexa metaphosphoric acid
Eight kinds of raw materials such as sodium, 1-hydroxy ethylidene-1,1-diphosphonic acid are proportionally added into normal pressure enamel reaction still.Slowly it is warming up to 55 DEG C.It is being stirred continuously
After 30 minutes, stop heating.Stirred in cooling, be cooled to normal temperature.Water is proportionally added into, it is stirring while adding, stir 20 minutes
After discharge, obtain corrosion-release scale-proof wax-removal viscosity-reducing agent.
Medicament prepared by the embodiment after just preparing in light yellow, and clear.But in room temperature, drying, cool place
Under conditions of place and just have white precipitate precipitation two days later, illustrate that this agent stability is bad.
By embodiment 5 and comparative example, a kind of oil recovery provided by the invention with corrosion-release scale-proof wax-removal agent through it is long when
Between place, do not produce precipitation.And the medicament in comparative example generates substantial amounts of precipitation after two day time is placed.By embodiment
1 to 5 understands, with corrosion-release scale-proof wax-removal agent, not only compatibility is good for a kind of oil recovery provided by the invention, has both met oil well to inhibition
The requirement of scale inhibition, requirement of the oil well to wax removal viscosity reduction is met again, and stability is high, and suitable large area in oilfield production pushes away
It is wide to use.
It is described above to be for only for ease of it will be understood by those skilled in the art that technical scheme, not limiting
The present invention.Within the spirit and principles of the invention, any modification, equivalent substitution and improvements made etc., it should be included in this
Within the protection domain of invention.
Claims (10)
1. one kind is recovered the oil and uses corrosion-release scale-proof wax-removal agent, it is characterised in that every 100 parts by weight are recovered the oil and use corrosion-release scale-proof wax-removal agent bag
Include:
2. as claimed in claim 1 recover the oil uses corrosion-release scale-proof wax-removal agent, it is characterised in that every 100 parts by weight oil recovery inhibition
Release scale-proof wax-removal agent includes:
3. as claimed in claim 1 recover the oil uses corrosion-release scale-proof wax-removal agent, it is characterised in that every 100 parts by weight oil recovery inhibition
Release scale-proof wax-removal agent includes:
4. as claimed in claim 1 recover the oil uses corrosion-release scale-proof wax-removal agent, it is characterised in that every 100 parts by weight oil recovery inhibition
Release scale-proof wax-removal agent includes:
5. as claimed in claim 1 recover the oil uses corrosion-release scale-proof wax-removal agent, it is characterised in that every 100 parts by weight oil recovery inhibition
Release scale-proof wax-removal agent includes:
6. as claimed in claim 1 recover the oil uses corrosion-release scale-proof wax-removal agent, it is characterised in that every 100 parts by weight oil recovery inhibition
Release scale-proof wax-removal agent includes:
7. as claimed in claim 1 recover the oil uses corrosion-release scale-proof wax-removal agent, it is characterised in that the fluorine carbon surfactant is
Fluorocarbon surfactant FN-3.
8. the preparation method as claimed in claim 1 recovered the oil with corrosion-release scale-proof wax-removal agent, it is characterised in that including following step
Suddenly:
First by oleic acid base hydroxyethyl imidazole quinoline, dodecyl benzyl dimethyl ammonium chloride, TEPA polyoxypropylene polyoxy second
Alkene ether is added in reactor, is slowly heated to temperature while stirring no more than 50 DEG C, is well mixed;
Backward reactor in add 1-hydroxy ethylidene-1,1-diphosphonic acid and ethylene glycol while stirring, be well mixed;
Add ATMP and ethylenediamine tetra-acetic acid while stirring into reactor again, be well mixed;
Then add fluorine carbon surfactant while stirring into reactor, stop adding after being well mixed, it is cold while stirring
But to room temperature;
Water is finally added while stirring, is well mixed, oil recovery corrosion-release scale-proof wax-removal agent is made;
Wherein, recover the oil and used in corrosion-release scale-proof wax-removal agent described in every 100 parts by weight, the addition of the oleic acid base hydroxyethyl imidazole quinoline
For 5-15 parts by weight;The addition of the dodecyl benzyl dimethyl ammonium chloride is 15-20 parts by weight;The hydroxy ethylidene two
The addition of phosphonic acids is 0.5-5 parts by weight;The addition of the ATMP is 0.5-2 parts by weight;The ethylenediamine
The addition of tetraacethyl is 0.5-5 parts by weight;The addition of the TEPA polyoxyethylene polyoxypropylene ether is 15-20 weights
Measure part;The addition of the fluorine carbon surfactant is 0.2-1 parts by weight;The addition of the ethylene glycol is 1-3 parts by weight;
Surplus is water.
9. the as claimed in claim 8 preparation method recovered the oil with corrosion-release scale-proof wax-removal agent, it is characterised in that it is described while stirring
It is slowly heated to 45-50 DEG C.
10. the preparation method recovered the oil as claimed in claim 8 or 9 with corrosion-release scale-proof wax-removal agent, it is characterised in that described slow
The speed that the temperature of heating rises is 3-5 DEG C/min.
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CN114456786A (en) * | 2018-09-18 | 2022-05-10 | 陕西信业科技开发有限公司 | Corrosion inhibitor for deep well oil gas gathering and transportation and preparation method thereof |
CN115261001A (en) * | 2021-04-29 | 2022-11-01 | 中国石油天然气股份有限公司 | Corrosion and scale inhibitor and preparation method thereof |
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CN113493683A (en) * | 2021-08-04 | 2021-10-12 | 东方宝麟科技发展(北京)有限公司 | Long-acting scale-inhibition wax-control composite synergist and preparation method thereof |
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