CN106146396A - Quinoline type derivant and corrosion inhibiting and descaling agent and application thereof and oil-field flooding pit shaft corrosion protection method of scale inhibition - Google Patents

Quinoline type derivant and corrosion inhibiting and descaling agent and application thereof and oil-field flooding pit shaft corrosion protection method of scale inhibition Download PDF

Info

Publication number
CN106146396A
CN106146396A CN201510205455.1A CN201510205455A CN106146396A CN 106146396 A CN106146396 A CN 106146396A CN 201510205455 A CN201510205455 A CN 201510205455A CN 106146396 A CN106146396 A CN 106146396A
Authority
CN
China
Prior art keywords
descaling agent
corrosion
quinoline
corrosion inhibiting
derivant
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
CN201510205455.1A
Other languages
Chinese (zh)
Other versions
CN106146396B (en
Inventor
王秀
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.)
Sinopec Research Institute of Petroleum Processing
China Petroleum and Chemical Corp
Original Assignee
Sinopec Research Institute of Petroleum Processing
China Petroleum and Chemical Corp
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 Sinopec Research Institute of Petroleum Processing, China Petroleum and Chemical Corp filed Critical Sinopec Research Institute of Petroleum Processing
Priority to CN201510205455.1A priority Critical patent/CN106146396B/en
Publication of CN106146396A publication Critical patent/CN106146396A/en
Application granted granted Critical
Publication of CN106146396B publication Critical patent/CN106146396B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D215/00Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems
    • C07D215/02Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom
    • C07D215/12Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom with substituted hydrocarbon radicals attached to ring carbon atoms
    • C07D215/14Radicals substituted by oxygen atoms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/26Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
    • C08G65/2618Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing nitrogen
    • 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
    • C09K8/52Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
    • 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
    • C09K8/54Compositions for in situ inhibition of corrosion in boreholes or wells
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B37/00Methods or apparatus for cleaning boreholes or wells
    • E21B37/06Methods or apparatus for cleaning boreholes or wells using chemical means for preventing or limiting, e.g. eliminating, the deposition of paraffins or like substances
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2650/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G2650/28Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type
    • C08G2650/50Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type containing nitrogen, e.g. polyetheramines or Jeffamines(r)

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Geology (AREA)
  • Mining & Mineral Resources (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Polymers & Plastics (AREA)
  • Medicinal Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • Health & Medical Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Abstract

The invention discloses the quinoline type derivant shown in a kind of Formulas I.The invention also discloses a kind of corrosion inhibiting and descaling agent and application thereof, described corrosion inhibiting and descaling agent contains quinoline type derivant, imidazoline type derivant, organic phosphine and zinc sulfate shown in Formulas I.The present invention further discloses a kind of oil-field flooding pit shaft corrosion protection method of scale inhibition, the method includes sending in oil-field flooding pit shaft described corrosion inhibiting and descaling agent.Corrosion inhibiting and descaling agent according to the present invention has good corrosion and scale inhibition performance, even if under relatively low using dosage, also can effectively suppress corrosion occurring and forming the trend of incrustation scale of the hardware contacted with high chlorine haline water under high temperature and high pressure environment, be with a wide range of applications in oil-field flooding pit shaft corrosion-mitigation scale-inhibition.

Description

Quinoline type derivant and corrosion inhibiting and descaling agent and application thereof and oil-field flooding pit shaft corrosion protection method of scale inhibition
Technical field
The present invention relates to a kind of quinoline type derivant, the invention still further relates to a kind of derivative containing described quinoline type The corrosion inhibiting and descaling agent of thing and application thereof, the invention further relates to a kind of oil-field flooding pit shaft corrosion protection scale inhibition side Method.
Background technology
At present, China's major part oil field comes into tail period stage, commonly used water flood recovery. In the case of water resource critical shortage, oil extraction-generated waste water re-injection had both solved the problem of shortage of water resources, again Solve and outside oil extraction-generated waste water, arrange the problem of environmental pollution caused.But, oil extraction-generated waste water contains substantial amounts of micro-life Thing, Ca2+、Mg2+、Cl-、SO4 2-Etc. perishable scale-forming ion, easily cause the corrosion and scaling of facility, Especially under water injection well pit shaft high-temperature and high-pressure conditions, corrode more serious with fouling condition.Corrosion and scaling is not Only make oil pipeline and auxiliary facility heavy corrosion be not normally functioning, and block oil reservoir hole, reduce Reservoir permeability, has a strong impact on the production exploitation in oil field.
Therefore, the corrosion inhibiter that exploitation can effectively suppress water filling pit shaft to corrode becomes study hotspot.
CN101629072A discloses a kind of oil field acidification high temperature inhibiter, including host and auxiliary agent, institute Stating host is N-Benzylmagnesium chloride quinoline, and its general structure is:
Host with the compound proportion of auxiliary agent is: 15-20%N-Benzylmagnesium chloride quinoline, 5-10% emulsifying agent, 3-5% propilolic alcohol, 20-30% formaldehyde and 35-57% ethanol, described emulsifying agent be fatty alcohol-polyoxyethylene ether, One in OPEO or its mixture.
CN1277241A discloses a kind of oil-field flooding corrosion inhibiter, and described corrosion inhibiter includes: (A) 70-80 Weight % imidazoline quaternary ammonium derivative, (B) 5-10 weight % alkynol, (C) 3-5 weight % alkali metal Iodide 1, (D) 0.5-1 weight % alkaline metal iodide 2, (E) 10-20 weight % solvent, wherein, Alkynol is C3-C6Alcohol, solvent is ethanol, isopropanol, ethylene glycol or water;Described imidazoline is quaternized to spread out Biological general structure is:
Wherein, R is C12-C20Alkyl or alkenyl.
CN102021583A discloses a kind of Inhibitor For Oil Well System, and this corrosion inhibiter is composed of the following components: 5-15 Weight %N-alkylamino-2-perfluoroalkylimidazquaternary quaternary ammonium salt, the hydrocarbon imidazoline of 0-5 weight % and derivative Thing, 10-20 weight % triethanolamine, 0-5 weight % carbamide and 55-85 weight % solvent, wherein, N- Shown in the molecular structure of alkylamino-2-perfluoroalkylimidazquaternary quaternary ammonium salt such as following formula (1) and (2), formula (1) With in formula (2), R1For CF3-(CF2)n, n=3-11, R2For C1-10Alkyl, C2-10Alkenyl, C3-7 One of cycloalkyl or any substituted aryl, aralkyl or heterocyclic base,
Wherein, n >=1;
Wherein, n >=1.
CN102167450A discloses a kind of oil field reinjection water special corrosion and scale inhibitor, by following weight hundred The raw material of proportion by subtraction is compounding to be formed: 5-20%2-phosphonate group-1,2,4-butane tricarboxylates, 15-30% poly, 10-25% oleic acid base bis-imdazoline corrosion inhibiter, 2-5% zinc sulfate, 3-10% sodium sulfite, surplus is for going Ionized water.
CN102321464A discloses a kind of for high water-cut stage oil well corrosion inhibiting and descaling agent, each composition weight Ratio is: the adjacent methylthiourea of 3.25-4.0% bis-, 12.5-13.5% ethylenediamine tetramethylene phosphonic acid salt, 8.0-8.5% Dodecyl butylamine Dimethyl sulfide, 3.0-3.25% myristyl tributyl chlorination, 15.0-16.2% DN-3212 acrylic acid, organic phosphine and sulfonic acid copolymer, 5.25-5.75%M-505A corrosion inhibiter, 6.85-7.25%SL-2 series corrosion inhibiting and descaling agent, 5.0-7.5% methanol, 3.4-3.75% hexamethylenamine, 0.05-0.055% vitamin A, remaining is water.
Although have been developed for some corrosion inhibiting and descaling agents for oil-field flooding pit shaft, but existing inhibition The composition of antisludging agent is complicated, adds the difficulty of execute-in-place, and environment is had substantially by some compositions Adverse effect;And, along with oil extraction difficulty strengthens, a large amount of use steam floodings improve recovery ratio, Requirement to corrosion inhibiting and descaling agent high temperature high voltage resistant performance is more and more higher, it is desirable to even if corrosion inhibiting and descaling agent is higher Temperature (such as 150 DEG C) under remain to stably play a role.
To sum up, need exploitation badly and there is the corrosion inhibiting and descaling agent of more preferable high temperature high voltage resistant performance.
Summary of the invention
It is an object of the invention to provide a kind of corrosion inhibiting and descaling agent, this corrosion inhibiting and descaling agent is in relatively low use agent Amount is lower can have excellence to the oil field reinjection water system being under high chlorine high salt and high temperature and high pressure environment Corrosion and scale inhibition performance.
According to the first aspect of the invention, the invention provides a kind of quinoline type derivant, this quinoline type The structural formula of derivant shown in formula I,
In Formulas I, A1For ethylene oxide substituents, R1For hydrogen or C1-C10Alkyl, R2For C1-C10 Alkyl or C7-C10Aralkyl, X1For halogen atom.
According to the second aspect of the invention, the invention provides a kind of corrosion inhibiting and descaling agent, this corrosion-mitigation scale-inhibition Agent contains at least one quinoline type derivant, at least one imidazoline type derivant, at least one organic phosphine And zinc sulfate,
The quinoline type derivant that described quinoline type derivant provides for the present invention,
Described imidazoline type derivant is selected from imidazoline type quaternary ammonium salt and bi-imidazoline.
According to the third aspect of the present invention, the invention provides described corrosion inhibiting and descaling agent to prevent at hardware Application in erosion scale inhibition.
According to the fourth aspect of the present invention, the invention provides a kind of oil-field flooding pit shaft corrosion protection scale inhibition side Method, the method includes sending in oil-field flooding pit shaft the corrosion inhibiting and descaling agent according to the present invention.
Corrosion inhibiting and descaling agent according to the present invention has good corrosion and scale inhibition performance, even if in relatively low use Under dosage, the hardware contacted with high chlorine haline water under high temperature and high pressure environment also can be effectively suppressed to send out The raw trend corroded and form incrustation scale, before having a wide range of applications in oil-field flooding pit shaft corrosion-mitigation scale-inhibition Scape.
Detailed description of the invention
According to the first aspect of the invention, the invention provides a kind of quinoline type derivant, this quinoline type The structural formula of derivant shown in formula I,
In Formulas I, A1For ethylene oxide substituents.
In Formulas I, the end group of ethylene oxide substituents is not particularly limited, such as, can be hydroxy-end capped Ethylene oxide substituents or alkyl are (such as C1-C5Alkyl, including C1-C5Straight chained alkyl and C3-C5 Branched alkyl, its instantiation can include but not limited to: methyl, ethyl, n-pro-pyl, isopropyl, Normal-butyl, sec-butyl, isobutyl group, the tert-butyl group, n-pentyl, isopentyl, tertiary pentyl and neopentyl) envelope The ethylene oxide substituents of end.In ethylene oxide substituents, the average repeat unit number of ethylene oxide unit Can be more than 1, preferably in the range of 1-30, more preferably in the range of 5-20.Ethylene oxide The average repeat unit number of unit use proton nmr spectra (1H NMR) determine.
In Formulas I, R1For hydrogen or C1-C10Alkyl.C1-C10Alkyl include C1-C10Straight chained alkyl And C3-C10Branched alkyl, its instantiation can include but not limited to: methyl, ethyl, n-pro-pyl, Isopropyl, normal-butyl, sec-butyl, isobutyl group, the tert-butyl group, n-pentyl, isopentyl, tertiary pentyl, new Amyl group, hexyl and isomer thereof, heptyl and isomer thereof, octyl group and isomer thereof and decyl and different Structure body.R1It is preferably C1-C6Alkyl, more preferably C1-C3Alkyl.
In Formulas I, R2For C1-C10Alkyl or C7-C10Aralkyl.C1-C10Alkyl include C1-C10 Straight chained alkyl and C3-C10Branched alkyl, its instantiation can include but not limited to: methyl, second Base, n-pro-pyl, isopropyl, normal-butyl, sec-butyl, isobutyl group, the tert-butyl group, n-pentyl, isopentyl, Tertiary pentyl, neopentyl, hexyl and isomer thereof, heptyl and isomer thereof, octyl group and isomer thereof and Decyl and isomer thereof.In the present invention, aralkyl refers to that at least one hydrogen atom in alkyl is taken by aryl The group that generation is formed.C7-C10The example of aralkyl can include but not limited to: phenyl methyl, phenyl Ethyl and phenyl n-pro-pyl.Preferably, R2For C1-C5Alkyl or C7-C10Aralkyl, more preferably For C7-C10Aralkyl, more preferably benzyl.
In Formulas I, X1For halogen atom, such as chlorine atom or bromine atoms, preferably chlorine atom.
In Formulas I, A1And R1The position of substitution be not particularly limited.Specifically, described quinoline type derives Thing can be Or
The instantiation of described quinoline type derivant can include but not limited to: 2-methyl-5-polyoxyethylene groups -quinoline type quaternary ammonium salt, 2-methyl-6-polyoxyethylene yl-quinoline type quaternary ammonium salt, 2-methyl-7-polyoxyethylene groups- Quinoline type quaternary ammonium salt, 2-methyl-8-polyoxyethylene yl-quinoline type quaternary ammonium salt, 3-methyl-5-polyoxyethylene groups- Quinoline type quaternary ammonium salt, 3-methyl-6-polyoxyethylene yl-quinoline type quaternary ammonium salt, 3-methyl-7-polyoxyethylene groups- Quinoline type quaternary ammonium salt, 3-methyl-8-polyoxyethylene yl-quinoline type quaternary ammonium salt, 4-methyl-6-polyoxyethylene groups- Quinoline type quaternary ammonium salt, 4-methyl-7-polyoxyethylene yl-quinoline type quaternary ammonium salt and 4-methyl-8-polyoxyethylene groups- Quinoline type quaternary ammonium salt.
Quinoline type derivant shown in Formulas I can use conventional method to prepare.Specifically, can be by corresponding Quinoline compound carry out quaternized, thus obtain the quinoline type derivant shown in Formulas I.Preferred in one Embodiment in, the quinoline type derivant shown in Formulas I can use the method that comprises the following steps to prepare: Under the conditions of quaterisation, by the quinoline compound shown in Formula II and the quaternizing agent shown in formula III Contact,
In Formula II, A1And R1Definition and Formulas I in A1And R1Definition identical;
R2-X1(formula III)
In formula III, R2And X1Definition and Formulas I in R2And X1Definition identical.
Quinoline compound shown in Formula II is commercially available, it would however also be possible to employ conventional method synthesizes.Specifically Ground, can use the method comprised the following steps to prepare the quinoline compound shown in Formula II: by formula IV institute The quinoline shown and oxirane carry out additive reaction,
In formula IV, R1Definition and Formulas I in R1Definition identical.
Mol ratio between quinoline shown in formula IV and oxirane can be according to the substituent A of Formula II1 The average repeat unit number of middle ethylene oxide unit selects.Usually, the quinoline shown in formula IV with The mol ratio of oxirane can be more than 1, preferably in the range of 1:1-30.
In course of reaction or after having reacted, one or more end-capping reagents can be added, with to Formula II In substituent A1The type of end group regulate and control.
Described additive reaction can 110-300 DEG C, carry out at a temperature of preferred 120-150 DEG C.Add When becoming reaction, the pressure in reactor can be 0.15-0.3MPa, preferably 0.15-0.3MPa.
Described additive reaction is carried out the most in the presence of a catalyst.Described catalyst can be inorganic base and/ Or organic base, preferably inorganic base.The instantiation of described catalyst can include but not limited to sodium hydroxide And potassium hydroxide.The consumption of catalyst can be for 0.1-1 weight % of quinoline shown in formula IV.
Quinoline compound shown in Formula II and the ratio between the quaternizing agent shown in formula III can be normal Rule select.Usually, the quinoline compound shown in Formula II and between the quaternizing agent shown in formula III Mol ratio can be 1:1.05-1.5, preferably 1:1.1-1.2.
Described quaterisation condition can conventional select, as long as be enough to the quinoline compound made shown in Formula II With the quaternizing agent generation quaterisation shown in formula III.Usually, quaterisation is permissible 40-100 DEG C, carry out at a temperature of preferred 50-80 DEG C.
Described quaterisation is preferably carried out at least one solvent.Described solvent can be both to have commonly used The quinoline compound shown in Formula II and the quaternizing agent shown in formula III can be dissolved, generation can be dissolved again The liquid substance of the quinoline type derivant shown in Formulas I.Preferably, described solvent is that low-carbon alcohols is (such as C1-C5 Fatty alcohol).It is highly preferred that described solvent is methanol and/or ethanol.The consumption of described solvent can be Conventional selection.Usually, the consumption of described solvent can be for the 1-10 of the quinoline compound shown in Formula II Times.
Quinoline type derivant according to the present invention has good corrosion and scale inhibition performance, can be used alone as delaying Erosion antisludging agent, it is also possible to be used as corrosion inhibiting and descaling agent with other components matching.
Thus, according to the second aspect of the invention, the invention provides a kind of corrosion inhibiting and descaling agent, this delays Erosion antisludging agent contain at least one quinoline type derivant, at least one imidazoline type derivant, at least one Organic phosphine and zinc sulfate, described quinoline type derivant is the quinoline provided according to the first aspect of the invention Quinoline type derivant.
In the present invention, " at least one " represents one or more.
Described quinoline type derivant and preparation method thereof has been carried out detailed description above, the most not Describe in detail again.
Described imidazoline type derivant is selected from imidazoline type quaternary ammonium salt and bi-imidazoline, preferably imidazoline type Quaternary ammonium salt.
Described imidazoline type quaternary ammonium salt be preferably selected from having structure shown in Formula IV imidazoline type quaternary ammonium salt and There is the imidazoline type quaternary ammonium salt of structure shown in Formula VII,
In Formula IV, R4And R5Identical or different, respectively C1-C10Alkyl, C7-C10Aralkyl, -R7OH、-R8NH2Or-R9COOH, R7、R8And R9It is respectively C1-C10Alkylidene.C1-C10 Alkyl include C1-C10Straight chained alkyl and C3-C10Branched alkyl, its instantiation can include but Be not limited to: methyl, ethyl, n-pro-pyl, isopropyl, normal-butyl, sec-butyl, isobutyl group, the tert-butyl group, N-pentyl, isopentyl, tertiary pentyl, neopentyl, hexyl and isomer thereof, heptyl and isomer thereof, Octyl group and isomer thereof and decyl and isomer thereof.C7-C10The example of aryl alkyl can include but not It is limited to: phenyl methyl, phenylethyl and phenyl n-pro-pyl.C1-C10Alkylidene include C1-C10Straight Chain alkylidene and C3-C10Branched alkylidene, its instantiation can include but not limited to methylene, Asia Ethyl, sub-n-pro-pyl, isopropylidene, sub-normal-butyl, sub-sec-butyl, isobutylidene, the sub-tert-butyl group, Sub-n-pentyl, isoamylidene, sub-tertiary pentyl, sub-neopentyl, hexylidene, heptamethylene, octylene and Decylene.
In Formula IV, R6For hydrogen or C8-C20Alkyl, C8-C20Alkyl in alkyl can be alkyl Or containing the alkyl of ethylene linkage, being preferably the alkyl containing ethylene linkage, more preferably alkenyl is (such as 1-alkene Base), more preferably C10-C20Alkenyl.
In Formula IV, X2For halogen atom, preferably chlorine atom.
In Formula VII, R10For hydrogen or C8-C20Alkyl, C8-C20Alkyl in alkyl can be alkyl Or containing the alkyl of ethylene linkage, being preferably the alkyl containing ethylene linkage, more preferably alkenyl is (such as 1-alkene Base), more preferably C10-C20Alkenyl.
In Formula VII, R11For C7-C10Aralkyl, its instantiation can include but not limited to: benzene Ylmethyl, phenylethyl and phenyl n-pro-pyl.
In Formula VII, X3For halogen atom, preferably chlorine atom.
It is highly preferred that described imidazoline type quaternary ammonium salt is selected from the imidazoline type season with structure shown in Formula VIII Ammonium salt and the imidazoline type quaternary ammonium salt with structure shown in Formula VIII I,
In Formula VIII, R12For C10-C20Alkenyl, preferably C15-C20Alkenyl;R13For benzyl Base, X4For chlorine atom;
In Formula VIII I, R14For benzyl;R15For C1-C10Alkylidene, preferably C1-C5Alkylidene, More preferably C1-C3Alkylidene;R16For C10-C20Alkenyl, preferably C15-C20Alkenyl; X5For chlorine atom.
It is further preferred that described imidazoline type quaternary ammonium salt is selected from the imidazoline with structure shown in Formula VIII Type quaternary ammonium salt and the imidazoline type quaternary ammonium salt with structure shown in Formula VIII I, in Formula VIII, R12It is 17 Thiazolinyl, in Formula VIII I, R15For ethylidene, R16It is 17 thiazolinyls.
Described imidazoline type quaternary ammonium salt can obtain by carrying out quaternized by imidazoline type compound.Institute State imidazoline type compound and can be selected from the compound shown in Formula V,
In Formula V, R17Can be hydrogen or C8-C20Alkyl, R18Can be hydrogen, C1-C10Alkyl, -R7OH、-R8NH2Or-R9COOH, R7、R8And R9It is respectively C1-C10Alkylidene.For R17, C8-C20Alkyl in alkyl can be alkyl or containing the alkyl of ethylene linkage, be preferably containing alkene The alkyl of key, more preferably alkenyl (such as 1-alkenyl), more preferably C10-C20Alkenyl.
Conventional quaternized method can be used to carry out quaternized by imidazoline type compound, such as halogenide Method, sulphuric acid ester process or acetic acid ester process.The present invention one preferred embodiment in, pass through halogenation Imidazoline type compound is carried out quaternized by thing method.This preferred embodiment in, as quaternized examination The halogenide of agent can be organohalogen compounds, such as: halogenated hydrocarbons is (such as C1-C10Halogenated alkane, C7-C10 Aralkyl halide), halogenated carboxylic acid is (such as C1-C10Halogenated carboxylic acid), halohydrin is (such as C1-C10 Haloalkyl alcohol) or halogenated amine (such as C1-C10Haloalkyl amine).
Described bi-imidazoline is commercially available.
Described organic phosphine refers to the organic compound in molecular structure containing C-P bond.Preferably, described Organic phosphine is containing hydroxyl and/or the organic phosphine of carboxyl in molecular structure.It is highly preferred that described organic phosphine is Containing carboxyl and/or the C of hydroxyl in molecular structure2-C12Representative examples of saturated aliphatic organic phosphine.It is further preferred that Described organic phosphine is selected from 2-phosphonobutane-1,2,4-tricarboxylic acids, hydroxyl-ethylene di 2 ethylhexyl phosphonic acid, 2-hydroxyl phosphino-second Acid and PAPE in one or more.Described PAPE can be such as PC-604。
According to the corrosion inhibiting and descaling agent of the present invention, quinoline type derivant, imidazoline type derivant, organic phosphine and The consumption of zinc sulfate can carry out suitable selection according to water quality.A kind of preferably embodiment party in the present invention In formula, relative to 100 weight portion quinoline type derivants, the content of described imidazoline type derivant is 1-60 Weight portion, preferably 10-55 weight portion, more preferably 30-50 weight portion, the content of described organic phosphine For 1-70 weight portion, preferably 10-60 weight portion, more preferably 30-50 weight portion, described zinc sulfate Content be 0.5-40 weight portion, preferably 10-35 weight portion, more preferably 20-30 weight portion.Root According to this preferred embodiment, can effectively suppress under higher temperature and pressure, with high salinity The component of aqueous mixture contact there is corrosion and form the trend of incrustation scale, be particularly well-suited to oil-field flooding The corrosion protection scale inhibition of pit shaft.
According to the third aspect of the present invention, the invention provides the corrosion inhibiting and descaling agent according to the present invention at gold Application in metal elements corrosion protection scale inhibition.
Application according to the present invention, described hardware can be the common structure needing to carry out corrosion-mitigation scale-inhibition Part, the hardware such as contacted with the aqueous mixture of high salinity, the mineralising of described aqueous mixture Degree can be more than 6000mg/L, such as 10000-300000mg/L.Described aqueous mixture is preferably height The aqueous mixture of chlorinity, its chlorinity can be more than 1000mg/L, as 10000-100000mg/L.Described salinity refers to various aniones and the total amount of cation in water.
Application according to the present invention, can will be dispersed in and hardware according to the corrosion inhibiting and descaling agent of the present invention In the aqueous mixture of contact, it is also possible to molten by being configured to corrosion inhibiter according to the corrosion inhibiting and descaling agent of the present invention Liquid, first carries out pretreatment with described corrosion inhibitor solution to the surface of hardware, makes preprocessed the most again Surface contact with described aqueous mixture, it is also possible to for the combination of above two method.
Application according to the present invention, described hardware can be various needs under high-temperature and high-pressure conditions with The hardware of high salinity aqueous solution contact, such as: oil-field flooding pit shaft.
According to the fourth aspect of the present invention, the invention provides a kind of oil-field flooding pit shaft corrosion protection scale inhibition side Method, the method includes sending in oil-field flooding pit shaft the corrosion inhibiting and descaling agent according to the present invention.
Can use conventional various methods that the corrosion inhibiting and descaling agent according to the present invention is sent into water injection well in oil fields In Tong.For example, it is possible to by the corrosion inhibiting and descaling agent of the present invention is dispersed in water filling;Can also be by this Bright corrosion inhibiting and descaling agent is configured to corrosion inhibitor solution (as the corrosion inhibiting and descaling agent of the present invention is dispersed in water filling In, form corrosion inhibitor solution), first with described corrosion inhibitor solution, the inner surface of water filling pit shaft is carried out pre-place Reason, then sends into water filling to water filling pit shaft;Above two Combination of Methods can also be used.
The consumption of described corrosion inhibiting and descaling agent can be conventional amount used.Corrosion inhibiting and descaling agent according to the present invention has Good anticorrosion-antiscaling effect, even under relatively low consumption, also can obtain high corrosion inhibition rate and scale inhibition Rate.The method according to the invention, the addition of described corrosion inhibiting and descaling agent can be 10-50mg/L, preferably For 12-40mg/L, more preferably 15-30mg/L.
Describe the present invention in detail below in conjunction with embodiment, but and be not so limited the scope of the present invention.
Embodiment 1-19 is used for the present invention is described.
Embodiment 1
(1) by 19.2g 2-methyl-5-hydroxyquinoline, (chemical reagent, ladder is uncommon likes (Shanghai) chemical conversion industry Development Co., Ltd) and catalyst (sodium hydroxide, 0.1g) join in reactor, close reactor, With air in nitrogen displacement still, it is warmed up to 120 DEG C with stirring, is slowly pressed into about 44g oxirane, Reaction two hours is continued afterwards under conditions of temperature is 120 DEG C and pressure is 0.15MPa.Take off after cooling Except solvent, the solid matter obtained is used13C-NMR is analyzed, and result display chemical shift is 67-72 Peak be the ehter bond formed, confirm that the solid matter that obtains is 2-methyl-5-polyoxyethylene yl-quinoline, its In, in polyoxyethylene groups the average repeat unit number of ethylene oxide unit be 8 (by1H-NMR determines).
(2) 45g 2-methyl-5-polyoxyethylene yl-quinoline and 50g methanol are joined be equipped with agitator, In the 250mL there-necked flask of Dropping funnel, reflux condensing tube and thermometer, it is warmed up to 50 with stirring DEG C, it is slowly added dropwise 13.0g benzyl chloride, after being added dropwise to complete, continues reaction 4 hours at 50 DEG C.Take off after cooling Except solvent, the solid matter C that will obtain13-NMR is analyzed, and confirms that the solid matter obtained is 2-methyl-5-polyoxyethylene yl-quinoline quaternary ammonium salt is (i.e.,Wherein, R1For Methyl, A1For polyoxyethylene groups, R2For benzyl, X1For chlorine).
Embodiment 2
(1) by 19.2g 3-methyl-8-hydroxyquinoline, (chemical reagent, ladder is uncommon likes (Shanghai) chemical conversion industry Development Co., Ltd) and catalyst (sodium hydroxide, 0.1g) join in reactor, close reactor, With air in nitrogen displacement still, it is warmed up to 120 DEG C with stirring, is slowly pressed into about 27g oxirane, Reaction two hours is continued afterwards under conditions of temperature is 120 DEG C and pressure is 0.15MPa.Take off after cooling Except solvent, the solid matter obtained is used13C-NMR is analyzed, and result display chemical shift is 67-72 Peak be the ehter bond formed, confirm that the solid that obtains is 3-methyl-8-polyoxyethylene yl-quinoline, wherein, In polyoxyethylene groups the average repeat unit number of ethylene oxide unit be 5 (by1H-NMR determines).
(2) 45g 3-methyl-8-polyoxyethylene yl-quinoline and 80g ethanol are joined be equipped with agitator, In the 250mL there-necked flask of Dropping funnel, reflux condensing tube and thermometer, it is warmed up to 78 with stirring DEG C, it is slowly added dropwise 13.0g benzyl chloride.Reaction 4 hours is continued at 78 DEG C after being added dropwise to complete.Take off after cooling Except solvent, the solid matter C that will obtain13-NMR is analyzed, and confirms that the solid matter obtained is 3-methyl-8-polyoxyethylene yl-quinoline quaternary ammonium salt is (i.e.,Wherein, R1For first Base, A1For polyoxyethylene groups, R2For benzyl, X1For chlorine).
Embodiment 3
(1) by 19.2g 4-methyl-7-hydroxyquinoline, (chemical reagent, ladder is uncommon likes (Shanghai) chemical conversion industry Development Co., Ltd) and catalyst (sodium hydroxide, 0.1g) join in reactor, close reactor, With air in nitrogen displacement still, it is warmed up to 120 DEG C with stirring, is slowly pressed into about 88g oxirane, Reaction two hours is continued afterwards under conditions of temperature is 120 DEG C and pressure is 0.15MPa.Take off after cooling Except solvent, solid matter will be obtained and use13C-NMR is analyzed, and result display chemical shift is 67-72 Peak be the ehter bond formed, confirm that the solid that obtains is 4-methyl-7-polyoxyethylene yl-quinoline, wherein, In polyoxyethylene groups the average repeat unit number of ethylene oxide unit be 16 (by1H-NMR determines).
(2) 45.0g 4-methyl-7-polyoxyethylene yl-quinoline and 80g ethanol are joined and be equipped with stirring In the 250mL there-necked flask of device, Dropping funnel, reflux condensing tube and thermometer, heat up with stirring To 80 DEG C, it is slowly added dropwise 13.0g benzyl chloride.Reaction 4 hours is continued at 80 DEG C after being added dropwise to complete.Cooling Rear desolvation, the solid matter C that will obtain13-NMR is analyzed, and confirms the solids obtained Matter be 4-methyl-7-polyoxyethylene yl-quinoline quaternary ammonium salt (i.e.,Wherein, R1For methyl, A1For polyoxyethylene groups, R2For benzyl, X1For chlorine).
Embodiment 4
(1) by 19.2g 4-methyl-8-hydroxyquinoline, (chemical reagent, ladder is uncommon likes (Shanghai) chemical conversion industry Development Co., Ltd) and catalyst (sodium hydroxide, 0.1g) join in reactor, close reactor, With air in nitrogen displacement still, it is warmed up to 120 DEG C with stirring, is slowly pressed into about 66g oxirane, Reaction two hours is continued afterwards under conditions of temperature is 120 DEG C and pressure is 0.15MPa.Take off after cooling Except solvent, the solid matter obtained is used13C-NMR is analyzed, and result display chemical shift is 67-72 Peak be the ehter bond formed, confirm that the solid that obtains is 4-methyl-8-polyoxyethylene yl-quinoline, wherein, In polyoxyethylene groups the average repeat unit number of ethylene oxide unit be 12 (by1H-NMR determines).
(2) 45g 4-methyl-8-polyoxyethylene yl-quinoline and 80g ethanol are joined be equipped with agitator, In the 250mL there-necked flask of Dropping funnel, reflux condensing tube and thermometer, it is warmed up to 78 with stirring DEG C, it is slowly added dropwise 13.0g benzyl chloride.Reaction 4 hours is continued at 78 DEG C after being added dropwise to complete.Take off after cooling Except solvent, the solid matter C that will obtain13-NMR is analyzed, and confirms that the solid matter obtained is 4-methyl-8-polyoxyethylene yl-quinoline quaternary ammonium salt is (i.e.,Wherein, R1For methyl, A1For polyoxyethylene groups, R2For benzyl, X1For chlorine).
Embodiment 5
2-methyl-5-polyoxyethylene-quinoline 45g embodiment 1 step (1) prepared and 50g methanol add Enter in the 250mL there-necked flask being equipped with agitator, Dropping funnel, reflux condensing tube and thermometer, It is warmed up to 60 DEG C with stirring, is slowly added dropwise 13.7g 1-n-butyl bromide, the temperature of 60 DEG C after being added dropwise to complete Lower continuation reacts 4 hours.Desolvation after cooling, the solid matter C that will obtain13-NMR carry out Analyze, confirm the solid matter that obtains be 2-methyl-5-polyoxyethylene yl-quinoline quaternary ammonium salt (i.e.,Wherein, R1For methyl, A1For polyoxyethylene groups, R2For normal-butyl, X1For bromine).
In following example and comparative example, following methods is used to evaluate corrosion mitigating effect.
(1) normal pressure static evaluation
Carrying out with reference to the method for regulation in oil and gas industry standard SY5273-91, concrete operations are: Being equipped with at politef lacing film, airway, catheter and the 250mL wide mouthed bottle of upper exhaustor In, hang up cleaning of having deoiled, the carbon steel test piece being dried and weighing;The air in bottle is got rid of with nitrogen, It is subsequently adding 200mL test water and corrosion inhibiting and descaling agent;Leakage test bottle, puts into internal temperature and is in examination Testing in the baking oven of temperature, constant temperature is placed 168 hours.
Temperature takes out test piece after being down to room temperature, washes away corrosion product with pickle, test piece is washed with clear water Totally, it is dried and weighs to constant weight, determine etching extent and use below equation to calculate corrosion inhibition rate.
(2) High Temperature High Pressure dynamic evaluation: hang up in the autoclave of 1000mL cleaning of having deoiled, The carbon steel test piece being dried and weigh;Get rid of the air in bottle with nitrogen, be subsequently adding 500mL and test water, Leakage test bottle, inflated with nitrogen is pressurized to test pressure (for 50kgf/cm2);With stirring, it is warmed up to examination Test temperature, constant temperature test 24 hours.
Take out test piece after being down to room temperature, wash away corrosion product with pickle, with clear water by test piece washes clean, It is dried and weighs to constant weight, determine etching extent and use below equation to calculate corrosion inhibition rate.
Wherein, moFor the corrosion weight of blank sample (that is, not adding the oil field reinjection water of corrosion inhibiting and descaling agent),
M is the corrosion weight after adding corrosion inhibiting and descaling agent.
In following example and comparative example, following methods is used to evaluate scale inhibition effect.
In 500mL volumetric flask, add corrosion inhibiting and descaling agent, be subsequently adding test water to 500mL, shake Even it is placed in 80 DEG C of waters bath with thermostatic control, stands 10 hours.After being down to room temperature, filter, take appropriate Cleaner liquid, titrates with EDTA standard solution, determines the calcium ion concentration in solution, uses following formula Calculate scale inhibition performance.
Wherein, V0Titrate for not adding the blank assay water EDTA standard solution of corrosion inhibiting and descaling agent Time the volume of EDTA that consumes;
V1For with the addition of consumption when the test water EDTA standard solution of corrosion inhibiting and descaling agent titrates The volume of EDTA.
The oil field reinjection water intermediate ion type and the content that use in following example and comparative example arrange in Table 1 Go out.
Table 1
Embodiment 6
2-methyl-5-the polyoxyethylene groups that in 1000mL assay flask prepared by addition 10mg embodiment 1- Quinoline quaternary ammonium salt, 5mg bi-imidazoline (purchased from triumph chemical plant, Qinhuangdao, the trade mark is DLPM), 3mg 2-phosphonobutane-1,2,4-tricarboxylic acids (purchased from Beijing Lin Hua water quality stabilizer factory) and 2mg zinc sulfate, use Oil field reinjection water adds to 1000mL, mix homogeneously, obtains testing water.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Comparative example 1
10mg bi-imidazoline is added (purchased from triumph chemical plant, Qinhuangdao, board in 1000mL assay flask Number be DLPM), 6mg 2-phosphonobutane-1,2,4-tricarboxylic acids and 4mg zinc sulfate, use oil field reinjection water Add to 1000mL, mix homogeneously, obtain testing water.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Comparative example 2
2-methyl-the 5-that in 1000mL assay flask prepared by addition 10mg embodiment 1 step (1) gathers Oxyethylene group-quinoline, 5mg bi-imidazoline (purchased from Qinhuangdao triumph chemical plant, the trade mark is DLPM), 3mg 2-phosphonobutane-1,2,4-tricarboxylic acids and 2mg zinc sulfate, add to 1000mL with oil field reinjection water, Mix homogeneously, obtains testing water.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Comparative example 3
Add 10mg 2-methyl-5-hydroxyquinoline in 1000mL assay flask, 5mg bi-imidazoline (is purchased From Qinhuangdao triumph chemical plant, the trade mark is DLPM), 3mg 2-phosphonobutane-1,2,4-tricarboxylic acids and 2mg Zinc sulfate, adds to 1000mL, mix homogeneously with oil field reinjection water, obtains testing water.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Comparative example 4
Add 10mg N-Benzylmagnesium chloride quinoline in 1000mL assay flask, 5mg bi-imidazoline (is purchased from Qinhuangdao triumph chemical plant, the trade mark is DLPM), 3mg 2-phosphonobutane-1,2,4-tricarboxylic acids and 2mg Zinc sulfate, adds to 1000mL, mix homogeneously with oil field reinjection water, obtains testing water.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Comparative example 5
8mg N-Benzylmagnesium chloride quinoline, 2mg linear alkyl phenol polyoxy second is added in 1000mL assay flask Alkene ether type nonionic surfactant (purchased from Bin Hua group, the trade mark is NP15), 5mg bi-imidazoline (are purchased From Qinhuangdao triumph chemical plant, the trade mark is DLPM), 3mg 2-phosphonobutane-1,2,4-tricarboxylic acids and 2mg Zinc sulfate, adds to 1000mL, mix homogeneously with oil field reinjection water, obtains testing water.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 7
Use method test preparation water same as in Example 6, except for the difference that, 2-phosphonobutane-1,2,4- Tricarboxylic consumption is 5mg.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 8
Use method test preparation water same as in Example 6, except for the difference that, 2-phosphonobutane-1,2,4- Tricarboxylic consumption is 1mg.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 9
Use method test preparation water same as in Example 6, except for the difference that, 2-phosphonobutane-1,2,4- Tricarboxylic consumption is 7mg.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 10
Using method test preparation water same as in Example 1, except for the difference that, the consumption of zinc sulfate is 3mg。
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 11
Using method test preparation water same as in Example 1, except for the difference that, the consumption of zinc sulfate is 4mg。
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 12
3-methyl-8-the polyoxyethylene groups that in 1000mL assay flask prepared by addition 10mg embodiment 2- Quinoline quaternary ammonium salt, 5mg 17 alkenyl imidazoline quaternary ammonium salt (Wherein, R12 It is 17 thiazolinyls, R13Benzyl, X4For chlorine atom), 3mg hydroxyl-ethylene di 2 ethylhexyl phosphonic acid is (purchased from Beijing woods Water quality stabilizer factory of China) and 2mg zinc sulfate, add to 1000mL with oil field reinjection water, mix homogeneously, Obtain testing water.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 13
Use the method test preparation water identical with embodiment 12, except for the difference that, 17 alkenyl imidazolines The consumption of quaternary ammonium salt is 6mg.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 14
4-methyl-7-the polyoxyethylene groups that in 1000mL assay flask prepared by addition 10mg embodiment 3- Quinoline quaternary ammonium salt, 5mg 17 thiazolinyl aminoethyl imidazoline quaternary ammonium salt (Wherein, R16It is 17 thiazolinyls, R15For ethylidene, R14For benzyl, X5For chlorine atom), 4mg 2-hydroxyl phosphino- Acetic acid (purchased from Beijing Lin Hua water quality stabilizer factory) and 2mg zinc sulfate, add to oil field reinjection water 1000mL, mix homogeneously, obtain testing water.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 15
Use the method test preparation water identical with embodiment 14, except for the difference that, 17 thiazolinyl aminoethyls The consumption of imidazoline quaternary ammonium salt is 3mg.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 16
Use the method test preparation water identical with embodiment 14, except for the difference that, 17 thiazolinyl aminoethyls The consumption of imidazoline quaternary ammonium salt is 1mg.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 17
Use the method test preparation water identical with embodiment 14, except for the difference that, 17 thiazolinyl aminoethyls The consumption of imidazoline quaternary ammonium salt is 0.5mg.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 18
4-methyl-8-the polyoxyethylene groups that in 1000mL assay flask prepared by addition 10mg embodiment 4- Quinoline quaternary ammonium salt, 5mg 17 thiazolinyl aminoethyl imidazoline quaternary ammonium salt (Wherein, R16It is 17 thiazolinyls, R15For ethylidene, R14For benzyl, X5For chlorine atom), 5mg polyhydric alcohol phosphoric acid Ester (PC-604, purchased from Beijing Lin Hua water quality stabilizer factory) and 2mg zinc sulfate, use oil field reinjection water Add to 1000mL, mix homogeneously, obtain testing water.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Embodiment 19
Use method test preparation water same as in Example 6, except for the difference that, 2-methyl-5-polyoxyethylene 2-methyl-5-polyoxyethylene yl-quinoline the quaternary ammonium salt of embodiment 5 preparation of the weight such as yl-quinoline quaternary ammonium salt use Replace.
This test water carries out normal pressure inhibition evaluation and high pressure inhibition evaluation, and result is respectively at table 2 and table 3 In list, this test water is carried out evaluation of anti-scale, result is listed in table 4.
Table 2
Numbering 50 DEG C of etching extent/mg 50 DEG C of corrosion inhibition rate/% 70 DEG C of etching extent/mg 70 DEG C of corrosion inhibition rate/%
Embodiment 6 1.2 94.6 1.2 95.2
Comparative example 1 12.5 43.4 14.8 41.0
Comparative example 2 4.0 81.9 5.0 80.1
Comparative example 3 9.8 55.7 12.3 51.0
Comparative example 4 7.2 67.4 9.1 63.7
Comparative example 5 7.1 67.9 8.5 66.1
Embodiment 7 1.1 95.0 1.3 94.8
Embodiment 8 1.2 94.6 1.4 94.4
Embodiment 9 1.3 94.1 1.4 94.4
Embodiment 10 1.1 95.0 1.3 94.8
Embodiment 11 1.3 94.1 1.4 94.4
Embodiment 12 1.0 95.5 1.2 95.2
Embodiment 13 1.2 94.6 1.3 94.8
Embodiment 14 1.3 94.1 1.4 94.4
Embodiment 15 1.4 93.7 1.3 94.8
Embodiment 16 1.6 92.8 1.5 94.0
Embodiment 17 1.8 91.9 1.9 92.4
Embodiment 18 1.1 95.0 1.3 94.8
Embodiment 19 1.4 93.7 1.5 94.0
Blank sample 22.1 / 25.1 /
Table 3
Numbering 120 DEG C of etching extent/mg 120 DEG C of corrosion inhibition rate/% 150 DEG C of etching extent/mg 150 DEG C of corrosion inhibition rate/%
Embodiment 6 1.5 95.1 1.6 95.1
Comparative example 1 15.1 50.5 17.3 46.9
Comparative example 2 5.9 80.7 7.9 75.8
Comparative example 3 13.0 57.4 13.5 58.6
Comparative example 4 9.8 67.9 10.4 68.1
Comparative example 5 10.1 66.9 10.9 66.6
Embodiment 7 1.5 95.1 1.5 95.4
Embodiment 8 1.7 94.4 1.8 94.5
Embodiment 9 2.0 93.4 2.2 93.3
Embodiment 10 1.4 95.4 1.5 95.4
Embodiment 11 1.8 94.1 1.9 94.2
Embodiment 12 1.6 94.8 1.2 96.3
Embodiment 13 1.8 94.1 1.5 95.4
Embodiment 14 1.3 95.7 1.4 95.7
Embodiment 15 1.4 95.4 1.4 95.7
Embodiment 16 1.7 94.4 1.9 94.2
Embodiment 17 2.6 91.5 2.5 92.3
Embodiment 18 1.5 95.1 1.5 95.4
Embodiment 19 1.8 94.1 1.8 94.5
Blank sample 30.5 / 32.6 /
Table 4
Numbering Scale inhibition performance/%
Embodiment 6 90.2
Comparative example 1 70.1
Comparative example 2 81.2
Comparative example 3 68.0
Comparative example 4 65.3
Comparative example 5 70.0
Embodiment 7 90.5
Embodiment 8 90.0
Embodiment 9 90.8
Embodiment 10 90.3
Embodiment 11 90.2
Embodiment 12 92.5
Embodiment 13 92.1
Embodiment 14 93.1
Embodiment 15 92.9
Embodiment 16 92.5
Embodiment 17 92.0
Embodiment 18 91.6
Embodiment 19 90.1
Table 2-4's as a result, it was confirmed that there is good corrosion and scale inhibition performance according to the corrosion inhibiting and descaling agent of the present invention, Even if under relatively low using dosage, also can effectively suppress under high temperature and high pressure environment with high chlorine haline water There is corrosion and form the trend of incrustation scale in the hardware of contact, has in oil-field flooding pit shaft corrosion-mitigation scale-inhibition Have wide practical use.

Claims (13)

1. a quinoline type derivant, the structural formula of this quinoline type derivant shown in formula I,
(Formulas I)
In Formulas I, A1For ethylene oxide substituents, R1For hydrogen or C1-C10Alkyl, R2For C1-C10 Alkyl or C7-C10Aralkyl, X1For halogen atom.
Quinoline type derivant the most according to claim 1, wherein, described quinoline type derivant is
Or
Quinoline type derivant the most according to claim 1 and 2, wherein, R1For C1-C6Alkane Base, preferably C1-C3Alkyl;
R2For C1-C5Alkyl or C7-C10Aralkyl, preferably C7-C10Aralkyl;
X1For chlorine atom.
4. according to the quinoline type derivant described in any one in claim 1-3, wherein, oxidation second In alkene substituent group, the average repeat unit number of ethylene oxide unit is more than 1, preferably in the scope of 1-30 In, more preferably in the range of 5-20.
5. a corrosion inhibiting and descaling agent, this corrosion inhibiting and descaling agent contains at least one quinoline type derivant, at least A kind of imidazoline type derivant, at least one organic phosphine and zinc sulfate,
Described quinoline type derivant is the quinoline type derivant in claim 1-4 described in any one,
Described imidazoline type derivant is selected from imidazoline type quaternary ammonium salt and bi-imidazoline.
Corrosion inhibiting and descaling agent the most according to claim 5, wherein, relative to 100 weight portion quinoline Type derivant, the content of described imidazoline type derivant is 1-60 weight portion, preferably 10-55 weight portion, More preferably 30-50 weight portion, the content of described organic phosphine is 1-70 weight portion, preferably 10-60 weight Amount part, more preferably 30-50 weight portion, the content of described zinc sulfate is 0.5-40 weight portion, is preferably 10-35 weight portion, more preferably 20-30 weight portion.
7. according to the corrosion inhibiting and descaling agent described in claim 5 or 6, wherein, described imidazoline type quaternary ammonium Salt is selected from having the imidazoline type quaternary ammonium salt of structure shown in Formula IV and having the imidazoles of structure shown in Formula VII Quinoline type quaternary ammonium salt,
(Formula IV)
In Formula IV, R4And R5Identical or different, respectively C1-C10Alkyl, C7-C10Aralkyl, -R7OH、-R8NH2Or-R9COOH, R7、R8And R9It is respectively C1-C10Alkylidene;R6For Hydrogen or C8-C20Alkyl, preferably C10-C20Alkenyl;X2For halogen atom;
(Formula VII)
In Formula VII, R10For hydrogen or C8-C20Alkyl, preferably C10-C20Alkenyl, R11For C7-C10Aralkyl, X3For halogen atom.
8. according to the corrosion inhibiting and descaling agent described in any one in claim 5-7, wherein, described organic Phosphine contains carboxyl and/or the organic phosphine of hydroxyl in molecular structure.
9. according to the corrosion inhibiting and descaling agent described in any one in claim 5-7, wherein, described organic Phosphine is selected from 2-phosphonobutane-1,2,4-tricarboxylic acids, hydroxyl-ethylene di 2 ethylhexyl phosphonic acid, 2-hydroxyl phosphino-acetic acid and many Unit alcohol phosphate ester in one or more.
10. in claim 5-9 corrosion inhibiting and descaling agent described in any one in hardware corrosion protection scale inhibition Application.
11. application according to claim 10, wherein, described hardware with salinity is The aqueous mixture contact of more than 6000mg/L.
12. 1 kinds of oil-field flooding pit shaft corrosion protection method of scale inhibition, the method includes to appoint in claim 5-9 A described corrosion inhibiting and descaling agent of anticipating is sent in oil-field flooding pit shaft.
13. methods according to claim 12, wherein, the consumption of described corrosion inhibiting and descaling agent is 10-50mg/L, preferably 12-40mg/L, more preferably 15-30mg/L.
CN201510205455.1A 2015-04-27 2015-04-27 Quinoline type derivative and corrosion inhibiting and descaling agent and its application and oil-field flooding pit shaft corrosion protection method of scale inhibition Active CN106146396B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510205455.1A CN106146396B (en) 2015-04-27 2015-04-27 Quinoline type derivative and corrosion inhibiting and descaling agent and its application and oil-field flooding pit shaft corrosion protection method of scale inhibition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510205455.1A CN106146396B (en) 2015-04-27 2015-04-27 Quinoline type derivative and corrosion inhibiting and descaling agent and its application and oil-field flooding pit shaft corrosion protection method of scale inhibition

Publications (2)

Publication Number Publication Date
CN106146396A true CN106146396A (en) 2016-11-23
CN106146396B CN106146396B (en) 2018-11-02

Family

ID=57347179

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510205455.1A Active CN106146396B (en) 2015-04-27 2015-04-27 Quinoline type derivative and corrosion inhibiting and descaling agent and its application and oil-field flooding pit shaft corrosion protection method of scale inhibition

Country Status (1)

Country Link
CN (1) CN106146396B (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107868043A (en) * 2017-11-14 2018-04-03 中国石油集团渤海钻探工程有限公司 A kind of quinoline quatemay ammonium inner salt type corrosion inhibiter and preparation method thereof
CN109306489A (en) * 2018-11-14 2019-02-05 上海应用技术大学 Functionalization quinolines liquid corrosion inhibitor, preparation method and application
CN110229653A (en) * 2019-06-11 2019-09-13 中国石油化工股份有限公司 A kind of resistance to CO2/H2The corrosion inhibiter and preparation method thereof of the shared corrosion of S
CN111777608A (en) * 2020-07-08 2020-10-16 湖北精瑜材料有限公司 Novel plant modified quinoline quaternary ammonium salt compound, preparation method and application
CN113526688A (en) * 2021-07-20 2021-10-22 国家石油天然气管网集团有限公司 Corrosion and scale inhibitor for oil transportation station and preparation method thereof
CN114086183A (en) * 2021-11-23 2022-02-25 天津新翔油气技术有限公司 Corrosion and scale inhibitor for oil and gas gathering and transportation and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2888399A (en) * 1953-04-01 1959-05-26 Petrolite Corp Process for inhibiting corrosion in oil and gas wells
US5322640A (en) * 1993-06-01 1994-06-21 Nalco Chemical Company Water soluble corrosion inhibitors
CN103992782A (en) * 2014-05-14 2014-08-20 华中科技大学 Acidizing corrosion inhibitor and preparation method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2888399A (en) * 1953-04-01 1959-05-26 Petrolite Corp Process for inhibiting corrosion in oil and gas wells
US5322640A (en) * 1993-06-01 1994-06-21 Nalco Chemical Company Water soluble corrosion inhibitors
CN103992782A (en) * 2014-05-14 2014-08-20 华中科技大学 Acidizing corrosion inhibitor and preparation method thereof

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
GURNEY0 . GUTEKUNSATN,等: "The 6-alkyloxyquinaldines", 《JOURNAL OF THE AMERICAN CHEMICAL SOCIETY》 *
杨宝和,等: "某些誉氮杂环化合物对价钢的缓蚀作用研究", 《高等学校化学学报》 *
蒋平,等: "喹啉型季铵盐缓蚀性能评价", 《油田化学》 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107868043A (en) * 2017-11-14 2018-04-03 中国石油集团渤海钻探工程有限公司 A kind of quinoline quatemay ammonium inner salt type corrosion inhibiter and preparation method thereof
CN109306489A (en) * 2018-11-14 2019-02-05 上海应用技术大学 Functionalization quinolines liquid corrosion inhibitor, preparation method and application
CN110229653A (en) * 2019-06-11 2019-09-13 中国石油化工股份有限公司 A kind of resistance to CO2/H2The corrosion inhibiter and preparation method thereof of the shared corrosion of S
CN111777608A (en) * 2020-07-08 2020-10-16 湖北精瑜材料有限公司 Novel plant modified quinoline quaternary ammonium salt compound, preparation method and application
CN111777608B (en) * 2020-07-08 2021-08-03 湖北精瑜材料有限公司 Novel plant modified quinoline quaternary ammonium salt compound, preparation method and application
CN113526688A (en) * 2021-07-20 2021-10-22 国家石油天然气管网集团有限公司 Corrosion and scale inhibitor for oil transportation station and preparation method thereof
CN114086183A (en) * 2021-11-23 2022-02-25 天津新翔油气技术有限公司 Corrosion and scale inhibitor for oil and gas gathering and transportation and preparation method thereof

Also Published As

Publication number Publication date
CN106146396B (en) 2018-11-02

Similar Documents

Publication Publication Date Title
CN106146396A (en) Quinoline type derivant and corrosion inhibiting and descaling agent and application thereof and oil-field flooding pit shaft corrosion protection method of scale inhibition
CN105733541B (en) Corrosion inhibiting and descaling agent composition and its application and oil-field flooding pit shaft corrosion protection method of scale inhibition
US10800963B2 (en) Pressure-reducing and injection-enhancing anti scaling agent for low-permeability water-injection well and preparation method thereof
CN104559983A (en) Corrosion inhibitor composition, corrosion inhibitor, application of corrosion inhibitor and anti-corrosion method of metal component
CN104711616B (en) A kind of aqua type metal cleaner and preparation method thereof
CN105712504B (en) A kind of corrosion inhibiting and descaling agent for acidic high-temperature gas water, preparation method and application
CN105670573B (en) The anti-boiling heat-conducting medium of environment-friendly type antifreeze and its application
CN102294132B (en) Defoamer for cleaning printed circuit board
CN101613598B (en) Inhibitor restraining H2S/CO2 corrosion and preparation method thereof
CN102321463A (en) Sulfur-containing bis-imidazoline type carbon dioxide corrosion inhibitor and preparation method thereof
CN107304162B (en) Gemini surfactant, preparation method and application thereof, oil displacement agent, oil displacement method of oil reservoir, oil stain cleaning agent and oil stain cleaning method
CN107418549A (en) A kind of compound acidification corrosion inhibitor of 120 ~ 140 DEG C of heatproof
CN108048065A (en) A kind of oil/gas well corrosion inhibiter and its preparation method and application
CN103352226A (en) Corrosion inhibitor used for preventing corrosion of brass
CN106148964B (en) A kind of corrosion inhibiter and its application and a kind of oil-field flooding pit shaft anti-corrosion method
CN105586595B (en) A kind of corrosion inhibiter and its application and a kind of oil-field flooding pit shaft anti-corrosion method
CN113416576A (en) Compound demulsifier and application thereof
CN111072165B (en) Composite scale and corrosion inhibitor and application thereof in low hard water
EP3110905A2 (en) Quaternary fatty acid esters as corrosion inhibitors
CN111039422B (en) Composite scale and corrosion inhibitor suitable for high-hardness water and application thereof
CN104557694B (en) Quinoline and its preparation method and application and corrosion inhibiting and descaling agent composition
CN104629927B (en) One kind peels off cleansing composition and its application method
CN105331448A (en) Stripping cleaning agent composition and usage method thereof
CN105331449B (en) A kind of stripping cleansing composition and its application method
CN104556426A (en) Preparation method for phosphorus-free compound corrosion and scale inhibitor

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant