CN116406670A - Sterilization corrosion inhibitor and preparation method and application thereof - Google Patents

Sterilization corrosion inhibitor and preparation method and application thereof Download PDF

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Publication number
CN116406670A
CN116406670A CN202111670899.4A CN202111670899A CN116406670A CN 116406670 A CN116406670 A CN 116406670A CN 202111670899 A CN202111670899 A CN 202111670899A CN 116406670 A CN116406670 A CN 116406670A
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corrosion inhibitor
substituted
unsubstituted
acid
group
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余华利
于磊
赵万伟
陈文�
汪枫
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Petrochina Co Ltd
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Petrochina Co Ltd
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Priority to PCT/CN2022/138527 priority patent/WO2023124953A1/en
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    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N43/00Biocides, pest repellants or attractants, or plant growth regulators containing heterocyclic compounds
    • A01N43/48Biocides, pest repellants or attractants, or plant growth regulators containing heterocyclic compounds having rings with two nitrogen atoms as the only ring hetero atoms
    • A01N43/501,3-Diazoles; Hydrogenated 1,3-diazoles
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01PBIOCIDAL, PEST REPELLANT, PEST ATTRACTANT OR PLANT GROWTH REGULATORY ACTIVITY OF CHEMICAL COMPOUNDS OR PREPARATIONS
    • A01P1/00Disinfectants; Antimicrobial compounds or mixtures thereof
    • 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
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F11/00Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
    • C23F11/04Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in markedly acid liquids
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F11/00Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
    • C23F11/08Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
    • C23F11/10Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
    • C23F11/14Nitrogen-containing compounds
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/30Against vector-borne diseases, e.g. mosquito-borne, fly-borne, tick-borne or waterborne diseases whose impact is exacerbated by climate change

Abstract

The invention discloses a sterilizing corrosion inhibitor and a preparation method and application thereof. The sterilizing corrosion inhibitor comprises the following components in percentage by weight: 10-90% of a compound of formula (I), 10-90% of an organic polar solvent, 0-20% of an auxiliary agent and the balance of water;

Description

Sterilization corrosion inhibitor and preparation method and application thereof
Technical Field
The invention relates to the field of petroleum and natural gas, in particular to a sterilization corrosion inhibitor and a preparation method and application thereof.
Background
In general, industrial water systems in the oil and gas field, and in particular industrial water in oil and gas field wells, have many different uses. Any water system, including its equipment and water, is susceptible to microbial contamination and scaling. Any metal surfaces in water systems are susceptible to corrosion, in part, due to microbial contamination and "microbiologically influenced corrosion". I.e. corrosion of the metal surface caused directly or indirectly by corrosion of the metal. And corrosion due to bacteria and their byproducts and metabolites on the metal surface, including in particular bacteria growing on the metal surface in biofilms. Bioerosion or bio-induced corrosion is typically associated with surface pitting, which results in faster corrosion damage than uniform corrosion.
Bioerosion or biologically induced chemical corrosion, typically caused by "sulfate-reducing bacteria" (sulfate-reducing bacteria SRB), is considered one of the major contributors to bioerosion under anaerobic conditions. It comprises a group of bacteria comprising at least 40 genus 137 species producing H 2 S, and bacteria using sulfate as terminal electron acceptor. Many SRBs are considered obligate anaerobes, meaning that they can temporarily tolerate low levels of oxygen, but in the presence of oxygen the cells are unable to normally metabolize and/or replicate. In addition, anaerobic conditions capable of supporting SRB growth can be created throughout the aerobic environment due to the microenvironment created within the bacterial biofilm/corrosion product layer. In addition, the bio-corrosion or bio-induced chemical corrosion also includes bio-corrosion or induced chemical corrosion of saprophytes, iron bacteria, and the like.
In general, SRB-induced bioerosion or SRB metabolization-induced H 2 S、CO 2 The chemical corrosion caused by the use of quaternary ammonium salts such as tetramethyl ammonium salt, tetraethyl ammonium salt, tetrapropyl ammonium salt, tetrabutyl ammonium salt, tetrahexyl ammonium salt and tetraoctyl ammonium salt is sterilized or controlled, but because the ammonium salt is cationic surfactant, a large amount of foam which is difficult to eliminate under the influence of air flow is generated with produced water during the use, and the foam not only can collect and transportThe process causes the influence of air resistance, and also can cause influence on production because the separator is incompletely separated.
Hydrogen sulfide and carbon dioxide are produced when organic matters are decomposed by bacteria in the process of forming petroleum and natural gas, are associated gas of petroleum and natural gas, and are faced with H in the development and production processes of many oil and gas fields at home and abroad 2 S/CO 2 Chemical corrosion and microbial corrosion present serious challenges for safe production.
At present, the filling of bactericides and corrosion inhibitors is a mainstream method for inhibiting corrosion and guaranteeing pipeline safety, wherein the bactericides are used for killing and controlling microorganisms, and the corrosion inhibitors mainly play a role in inhibiting electrochemical corrosion. Patent application CN106719681A discloses an oilfield sterilization corrosion inhibitor and a preparation method thereof, patent application CN110273157A discloses a corrosion inhibitor with sterilization and scale inhibition functions and a preparation method thereof, patent application CN104628097A discloses a composition for the sterilization corrosion inhibitor, and patent application CN109971447A discloses a sterilization corrosion inhibitor for oil well gathering and transportation and sewage treatment systems and a preparation method thereof. Patent application JP2006348079A discloses a diamine alkoxy compound which has bactericidal, low foaming and corrosion inhibiting properties. Patent application RU2255141C1 discloses a bactericidal corrosion inhibitor for oilfield hydrogen sulfide-mineralized aqueous media, which is prepared by reacting a C8-C18 primary fatty amine with a phosphorus-containing acid derivative, particularly a product of phosphoric acid and a polyol. Patent application RU2259393C2 discloses a bactericidal corrosion inhibitor of an industrial detergent composition with anti-corrosive and bactericidal properties, which is prepared by reacting N, N-methyl methane diamine with alkyl and alkenyl chlorides, and can be used in all industrial fields where metal surfaces are attached by organic oil stains including oil gas, lubricating oil, latex contents, asphalt, tar, paraffin and the like. Patent application US9802908B2 discloses that an ethylbenzyl quaternary ammonium salt of amino amide has bactericidal performance and can be used as an oil field cleaning soap clay cleaning agent and a corrosion inhibitor. The techniques can play a certain role in sterilization and corrosion inhibition.
However, the prior art suffers from at least the following problems: 1) Most of the existing bactericidal corrosion inhibitor products are compositions, namely, the corrosion inhibitor is mixed with the bactericide. The product performance is difficult to be improved on the basis of the original corrosion inhibitor and bactericide. 2) Most of the existing sterilizing corrosion inhibitors sold in the market and most applied are based on quaternary ammonium salt, wherein the quaternary ammonium salt is a cationic surfactant, and a large amount of foam which is difficult to eliminate can be generated with produced water under the influence of air flow in the use process, and the foam not only can cause air resistance influence on the gathering and transportation process, but also can cause influence on production because of incomplete separation of a separator.
Disclosure of Invention
In order to solve at least one of the technical problems, the invention provides a sterilizing corrosion inhibitor, and a preparation method and application thereof. The sterilization corrosion inhibitor has a novel structure and has the functions of corrosion inhibition and sterilization. Compared with a single aldehyde bactericide, the bactericidal corrosion inhibitor can effectively reduce the tolerance of various strains; compared with quaternary ammonium salt bactericide, the disinfectant has obviously reduced foam and high bactericidal power.
In order to achieve the above purpose, the present invention adopts the following technical scheme:
the invention provides a sterilization corrosion inhibitor, which comprises the following components in percentage by weight: 10-90% of a compound of formula (I), 10-90% of an organic polar solvent, 0-20% of an auxiliary agent and the balance of water;
Figure BDA0003449464480000031
wherein R is 1 One selected from the group consisting of a substituted or unsubstituted C1-C20 linear or branched alkyl group, a C1-C20 alkoxy group, a substituted or unsubstituted C1-C20 linear or branched alkenyl group, a C1-C20 alkylthio group, a substituted or unsubstituted C3-C20 cycloalkyl group, a substituted or unsubstituted C6-C30 aryl group, and a substituted or unsubstituted C2-C30 heteroaryl group;
R 2 selected from H, substituted or unsubstituted C1-C20 straight or branched alkyl, C1-C20 alkoxy, substituted or unsubstituted C1-C20 straight or branched alkenyl, C1-C20 alkylthio, substituted or unsubstituted C3-C20 cycloalkyl, substituted or unsubstituted C6-C30 aryl, substitutedOr one of unsubstituted C2-C30 heteroaryl;
X - selected from COO - 、SO 3 - 、H 2 PO 4 - Or HSO 4 -
The sterilizing corrosion inhibitor according to the present invention, preferably, the R 1 Selected from the group consisting of substituted or unsubstituted C1-C20 linear or branched alkyl groups, and substituted or unsubstituted C1-C20 linear or branched alkenyl groups.
The sterilizing corrosion inhibitor according to the present invention, preferably, the R 1 Selected from substituted or unsubstituted C1-C20 straight or branched alkyl groups.
The sterilizing corrosion inhibitor according to the present invention, preferably, the R 1 Selected from the group consisting of substituted or unsubstituted C6-C15 linear alkyl groups. More preferably, the R 1 Selected from the group consisting of substituted or unsubstituted C6, C7, C8, C9, C10, C11, C12, C13, C14, C15 straight chain alkyl groups.
The substituent in the above substituted group may be a hydroxyl group, a mercapto group, an amine group, a carbonyl group, an alkenyl group, an alkynyl group, an alkyl group, or the like.
The sterilizing corrosion inhibitor according to the present invention, preferably, the R 1 Is straight-chain undecyl.
The sterilizing corrosion inhibitor according to the invention, preferably, R 2 Selected from H, substituted or unsubstituted C1-C20 straight-chain or branched alkyl, and substituted or unsubstituted C6-C30 aryl.
The sterilizing corrosion inhibitor according to the invention, preferably, R 2 One of H, C-C20 linear or branched alkyl, mercapto-substituted C1-C20 linear or branched alkyl and alkyl-substituted C6-C30 aryl.
The sterilizing corrosion inhibitor according to the invention, preferably, R 2 Is H, methyl, mercaptomethyl or p-tolyl.
According to the sterilizing corrosion inhibitor of the present invention, preferably, the organic polar solvent includes one or a combination of two or more of alcohols, amides, nitriles, pyridines, ketones, ethers, and aromatic compounds.
Preferably, the alcohols include methanol, ethanol, propanol, isopropanol, butanol, methylethanol, isobutanol, pentanol, isopentanol, ethylene glycol, 2-methyl-1-butanol.
The bactericidal corrosion inhibitor according to the present invention preferably, the auxiliary agent comprises one or a combination of two or more of thiourea, thiazole, silicone and derivatives thereof, halogenated hydrocarbons, halogenated olefins and halogenated aromatic hydrocarbons.
According to the bactericidal corrosion inhibitor of the invention, preferably, the auxiliary agent is methyl iodide or chloropropene.
According to the bactericidal corrosion inhibitor of the present invention, preferably, the mass percentage of the compound of formula (I) is 20-25%, the mass percentage of the organic polar solvent is 20-30%, and the mass percentage of the auxiliary agent is 0-10%, more preferably 5-10%.
The invention also provides a preparation method of the sterilization corrosion inhibitor, which comprises the following steps:
r is R 1 Corresponding imidazole compound and organic acid R 2 And (3) after the X reacts in the organic polar solvent, adding an auxiliary agent to continue the reaction, and then adding water to obtain the sterilizing corrosion inhibitor.
According to the production method of the present invention, preferably, the acid is selected from an organic acid including acetic acid (CH 3 COOH,R 2 Is CH 3 ,X - Is COO - ) Thioglycollic acid
Figure BDA0003449464480000041
R 2 For SHCH 2 ,X - Is COO - ) And p-toluenesulfonic acid (+)>
Figure BDA0003449464480000042
R 2 Is p-tolyl, X - Is SO 3 - ) The method comprises the steps of carrying out a first treatment on the surface of the The inorganic acid includes phosphoric acid (H) 3 PO 4 ,R 2 Is H, X - Is H 2 PO 4 - ) And sulfuric acid (H) 2 SO 4 ,R 2 Is H, X - Is HSO 4 - )。
According to the preparation method of the present invention, preferably, the imidazole compound is reacted with the organic acid at a temperature of 10 to 100 ℃, more preferably 40 ℃.
According to the preparation method of the present invention, preferably, the imidazole compound is reacted with an acid R 2 The reaction time of X is 0.5-24 hours.
According to the preparation method of the present invention, preferably, the imidazole compound is reacted with an acid R 2 The reaction temperature of X is 20-80 ℃ and the time is 0.5-24 hours.
According to the preparation method of the invention, preferably, the temperature of the continuous reaction of adding the auxiliary agent is 40-80 ℃ and the time is 2-8 hours. More preferably, the temperature is 60℃for a period of 4 hours.
According to the preparation method of the present invention, preferably, the imidazole compound and the acid R 2 -X has a molar ratio of 1: (1 to 6), more preferably 1: (2 to 5), more preferably 1: (3-4), e.g., 1:1.
The polar solvent accounts for 10-90% of the mass of the reaction system, such as 80-90%, 70-90%, 60-90% and 50-90%.
According to the preparation method of the present invention, the auxiliary agent preferably accounts for 0-20% by mass of the reaction system, more preferably 0-10% by mass, and still more preferably 5-10% by mass.
In a further aspect, the invention provides the use of the above antimicrobial corrosion inhibitor in the protection of oil and gas fields against microbial corrosion or against chemical corrosion.
The microorganisms in the microbial corrosion comprise one or more than two of sulfate reducing bacteria, saprophytic bacteria and iron bacteria. The chemical etching includes H 2 S、CO 2 Corrosion caused.
The compound shown in the formula (I) and the bactericidal corrosion inhibitor prepared by the compound can be quickly adsorbed on the metal surface and the bacterial surface, and has good corrosion inhibition capability, bactericidal capability and bacteriostatic capability, and as shown in the embodiment of the invention, the corrosion rate mainly of hydrogen sulfide corrosion or carbon dioxide corrosion can be controlled below 0.076mm/a, sulfate Reducing Bacteria (SRB) can be effectively killed, and the bactericidal rate is more than 99%.
In terms of sterilization mechanism, effective sterilization molecules generally comprise hydrophilic cationic groups and hydrophobic alkyl chains, the mechanism is mainly that antibacterial polymers are firstly adhered to the surface of bacteria through electrostatic interaction, then substituted alkyl groups on the molecules penetrate cell membranes through hydrophobic interaction to cause bacterial death, and therefore, the effective high-molecular bactericide should comprise three elements: (1) must be in sufficient contact with the cells; (2) sufficient cationic charge must be present to promote adhesion to the microbial cell membrane; (3) a portion of the hydrophobic chains must be available to adsorb and fuse into the porous cell membrane interior. Because the surface of the bacterial cell membrane is negatively charged, the compound shown in the formula (I) is an ionic compound with positive charges, and can be adsorbed on the surface of the bacterial cell membrane through electrostatic interaction, and the hydrophobic group part of the compound penetrates through the cell membrane to enter the cell interior to play a role in sterilization. The imidazole derivative is a broad-spectrum bactericide, but because of poor water solubility and poor practical application, 2-undecylimidazole has weak alkalinity and can react with organic acid to generate ionic compounds with positive charges, the water solubility of the ionic compounds is enhanced, the ionic compounds play a role in adsorbing and sterilizing, and in addition, S, P in the organic acid can enhance the performance in corrosion inhibition.
Detailed Description
In order to more clearly illustrate the present invention, the present invention will be further described with reference to preferred embodiments. It is to be understood by persons skilled in the art that the following detailed description is illustrative and not restrictive, and that this invention is not limited to the details given herein.
All numerical designations of the invention (e.g., temperature, time, concentration, weight, etc., including ranges for each) can generally be approximations that vary (+) or (-) as appropriate in 0.1 or 1.0 increments. All numerical designations are to be understood as preceded by the term "about".
Example 1
The embodiment provides a sterilization corrosion inhibitor, which is prepared by the following method:
2-undecylimidazole (0.1 mol, 22.2 g), acetic acid (0.1 mol, 6.1 g) and 28.0g of butanol were mixed, stirred at 40℃until homogeneous, and then 56.3g of water was added to obtain the final drug 1.
Example 2
The embodiment provides a sterilization corrosion inhibitor, which is prepared by the following method:
2-undecylimidazole (0.1 mol, 22.2 g), thioglycollic acid (0.1 mol, 9.2 g) and 32.0g of ethylene glycol were mixed, stirred at 40℃until homogeneous, and then 63.0g of water was added to obtain the final drug 2.
Example 3
The embodiment provides a sterilization corrosion inhibitor, which is prepared by the following method:
2-undecylimidazole (0.1 mol, 22.2 g), p-toluenesulfonic acid (0.1 mol, 17.2 g) and 40.0g of isopropyl alcohol were mixed, stirred at 40℃until homogeneous, and then 80.0g of water was added to obtain final drug 3.
Example 4
The embodiment provides a sterilization corrosion inhibitor, which is prepared by the following method:
2-ethylimidazole (0.1 mol, 9.6 g), thioglycollic acid (0.1 mol, 9.2 g) and 18.8g butanol were mixed, stirred at 40℃until homogeneous, and then 37.6g water was added to obtain final drug 4.
Example 5
The embodiment provides a sterilization corrosion inhibitor, which is prepared by the following method:
2-undecylimidazole (0.1 mol, 22.2 g), thioglycollic acid (0.1 mol, 9.2 g) and 32.0g of ethylene glycol were mixed, stirred at 40℃until homogeneous, then 14.2g of methyl iodide was added, stirred at 60℃for 4 hours, and then 78.0g of water was added, to obtain the final drug 5.
Example 6
The embodiment provides a sterilization corrosion inhibitor, which is prepared by the following method:
2-undecylimidazole (0.1 mol, 22.2 g), phosphoric acid (0.1 mol, 9.8 g) and 32.0g of ethylene glycol were mixed, stirred at 40℃until homogeneous, then 14.2g of methyl iodide was added, stirred at 60℃for 4 hours, and then 78.0g of water was added, to obtain the final drug 6.
Example 7
The embodiment provides a sterilization corrosion inhibitor, which is prepared by the following method:
2-undecylimidazole (0.1 mol, 22.2 g), sulfuric acid (0.1 mol, 9.8 g) and 32.0g of ethylene glycol were mixed, stirred at 40℃until homogeneous, 7.7g of chloropropene was added, stirred at 60℃for 4 hours, and then 72.0g of water was added to obtain the final drug 7.
Example 8
The embodiment provides a sterilization corrosion inhibitor, which is prepared by the following method:
2-undecylimidazole (0.1 mol, 22.2 g), acetic acid (0.1 mol, 6.1 g) and 28.0g of butanol were mixed, stirred at 40℃until homogeneous, 7.7g of chloropropene was added, stirred at 60℃for 4 hours, and then 64.0g of water was added to obtain the final drug 8.
Application example 1
The bactericidal corrosion inhibitors obtained in examples 1 to 8 were evaluated. The specific evaluation process comprises the following steps:
performing sterilization tests on SRB-containing bacterial water samples by using the medicaments 1-8 respectively, wherein the concentration of a sterilization corrosion inhibitor is 100mg/L and 50mg/L, culturing the SRB-containing bacterial water sample for 24 hours at 25 ℃ in an anaerobic environment after the addition of the sterilization agent, determining the bacterial content by referring to a SY/T0532 oilfield injection water bacteria analysis method (sterilization dilution method), and calculating the sterilization rate, wherein the result is shown in the table 1, and the calculation formula of the sterilization rate is as follows:
Figure BDA0003449464480000071
wherein:
x-sterilization rate,%;
a 2 number of bacteria after sterilization, number of bacteria/mL;
a 1 blank bacterial count, number/mL.
TABLE 1
Sterilization corrosion inhibitor Concentration of test agent, ppm SRB bacterial count, individual Sterilization rate of%
Blank space - 2.5×10 2 -
Medicament 1 100 0 99.9
Medicament 2 100 0 99.9
Medicament 3 100 0 99.9
Medicament 4 100 0 99.9
Medicament 5 50 0 100.0
Medicament 6 50 0 100.0
Medicament 7 50 0 100.0
Medicament 8 50 0 100.0
As is clear from Table 1, the sterilizing rate of the traditional Chinese medicine preparation 1-preparation 4 in the examples is more than 99.9%, the use concentration of the preparation 5-preparation 8 added with the auxiliary agent in the examples is reduced by one time, the sterilizing effect is improved, and the sterilizing rate reaches 100%. Therefore, the sterilizing corrosion inhibitor provided by the embodiment of the invention has good sterilizing performance.
Application example 2
This application example was used for evaluating the bactericidal corrosion inhibitors obtained in examples 1 to 8, respectively. The specific evaluation process comprises the following steps:
500ppm CO was measured using agent 1-agent 8, respectively 2 The corrosion test is carried out on a 5% sodium chloride water sample, the sterilization corrosion inhibitor is 100mg/L in concentration, the corrosion material is L360N, after the water sample is placed for 72 hours in an anaerobic environment at 40 ℃, the corrosion inhibitor technical requirement and evaluation method for SY/T7437 natural gas gathering and transportation are referred, and the corrosion rate is calculated, and the results are shown in Table 2. The corrosion rate was calculated as follows:
Figure BDA0003449464480000081
wherein:
vc-the uniform corrosion rate in millimeters per year (mm/a);
m-weight loss of hanging piece, the unit is gram (g);
s-exposed area of the hanging piece in square centimeter (cm) 2 );
t-experimental time in hours (h);
ρ -relative density of the hanging sheet in grams per cubic centimeter (g/cm) 3 )。
TABLE 2
The sterilizing corrosion inhibitor provided in the embodiment Concentration of test agent, ppm Corrosion rate, mm/a
Blank space - 0.3890
Medicament 1 100 0.0646
Medicament 2 100 0.0514
Medicament 3 100 0.0580
Medicament 4 100 0.0554
Medicament 5 100 0.0488
Medicament 6 100 0.0660
Medicament 7 100 0.0673
Medicament 8 100 0.0422
As is clear from Table 2, the corrosion rates of the agents 1 to 8 were not more than 0.076 mm/a. Therefore, the sterilizing corrosion inhibitor provided by the embodiment of the invention has good corrosion inhibition performance.
It should be understood that the foregoing examples of the present invention are provided merely for clearly illustrating the present invention and are not intended to limit the embodiments of the present invention, and that various other changes and modifications may be made therein by one skilled in the art without departing from the spirit and scope of the present invention as defined by the appended claims.

Claims (24)

1. The sterilizing corrosion inhibitor is characterized by comprising the following components in percentage by weight: 10-90% of a compound of formula (I), 10-90% of an organic polar solvent, 0-20% of an auxiliary agent and the balance of water;
Figure FDA0003449464470000011
wherein R is 1 One selected from the group consisting of a substituted or unsubstituted C1-C20 linear or branched alkyl group, a C1-C20 alkoxy group, a substituted or unsubstituted C1-C20 linear or branched alkenyl group, a C1-C20 alkylthio group, a substituted or unsubstituted C3-C20 cycloalkyl group, a substituted or unsubstituted C6-C30 aryl group, and a substituted or unsubstituted C2-C30 heteroaryl group;
R 2 one selected from H, substituted or unsubstituted C1-C20 straight-chain or branched alkyl, C1-C20 alkoxy, substituted or unsubstituted C1-C20 straight-chain or branched alkenyl, C1-C20 alkylthio, substituted or unsubstituted C3-C20 cycloalkyl, substituted or unsubstituted C6-C30 aryl and substituted or unsubstituted C2-C30 heteroaryl;
X - selected from COO - 、SO 3 - 、H 2 PO 4 - Or HSO 4 -
2. The bactericidal corrosion inhibitor according to claim 1, wherein R 1 Selected from the group consisting of substituted or unsubstituted C1-C20 linear or branched alkyl groups, and substituted or unsubstituted C1-C20 linear or branched alkenyl groups.
3. The bactericidal corrosion inhibitor according to claim 2, wherein R 1 Selected from substituted or unsubstituted C1-C20 straight or branched alkyl groups.
4. A bactericidal corrosion inhibitor according to claim 3, wherein R 1 Selected from the group consisting of substituted or unsubstituted C6-C15 linear alkyl groups.
5. The bactericidal corrosion inhibitor according to claim 4, wherein R 1 Is straight-chain undecyl.
6. The bactericidal corrosion inhibitor according to claim 1, wherein R 2 Selected from H, substituted or unsubstituted C1-C20 straight or branched alkyl, substituted or unsubstitutedAnd C6-C30 aryl of the generation.
7. The bactericidal corrosion inhibitor according to claim 6, wherein R 2 One of H, C-C20 linear or branched alkyl, mercapto-substituted C1-C20 linear or branched alkyl and alkyl-substituted C6-C30 aryl.
8. The bactericidal corrosion inhibitor according to claim 7, wherein R 2 Is H, methyl, mercaptomethyl or p-tolyl.
9. The bactericidal corrosion inhibitor according to claim 1, wherein the organic polar solvent comprises one or a combination of two or more of alcohols, amides, nitriles, pyridines, ketones, ethers, and aromatic compounds.
10. The bactericidal corrosion inhibitor of claim 9 wherein the organic polar solvent is selected from the group consisting of alcohols.
11. The corrosion and disinfection agent of claim 10, wherein said alcohol comprises methanol, ethanol, propanol, isopropanol, butanol, methylethanol, isobutanol, pentanol, isopentanol, ethylene glycol, 2-methyl-1-butanol.
12. The corrosion and disinfection agent of claim 1, wherein said adjuvant comprises one or a combination of two or more of thiourea, thiazole, silicone and derivatives thereof, halogenated alkanes, halogenated alkenes and halogenated arenes.
13. The bactericidal corrosion inhibitor of claim 12, wherein the auxiliary is methyl iodide or chloropropene.
14. The bactericidal corrosion inhibitor according to claim 1, wherein the mass percentage of the compound of formula (I) is 20-25%, the mass percentage of the organic polar solvent is 20-30%, and the mass percentage of the auxiliary agent is 0-10%.
15. A method of preparing the bactericidal corrosion inhibitor of any of claims 1 to 14, comprising the steps of:
r is R 1 Corresponding imidazole compound and acid R 2 And (3) after the X reacts in the organic polar solvent, adding an auxiliary agent to continue the reaction, and then adding water to obtain the sterilizing corrosion inhibitor.
16. The method of claim 15, wherein the acid is acetic acid, thioglycollic acid, p-toluenesulfonic acid, phosphoric acid or sulfuric acid.
17. The method according to claim 15, wherein the imidazole compound is reacted with an acid R 2 The temperature at which X is reacted is from 10 to 100 ℃.
18. The method according to claim 15, wherein the imidazole compound is reacted with an acid R 2 The reaction time of X is 0.5-24 hours.
19. The method according to claim 15, wherein the imidazole compound is reacted with an acid R 2 The reaction temperature of X is 20-80 ℃ and the time is 0.5-24 hours.
20. The process of claim 15, wherein the addition of the auxiliary agent is carried out at a temperature of 40 to 80 ℃ for 2 to 8 hours.
21. The preparation method according to claim 15, wherein the imidazole compound and the acid R 2 -X has a molar ratio of 1: (1-6).
22. The preparation method according to claim 15, wherein the organic polar solvent accounts for 10-90% of the mass of the reaction system.
23. The preparation method according to claim 15, wherein the auxiliary agent accounts for 0-20% of the mass of the reaction system.
24. Use of the bactericidal corrosion inhibitor of any of claims 1 to 14 for microbial or chemical corrosion protection in oil and gas fields.
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US3639629A (en) * 1969-02-17 1972-02-01 Stauffer Chemical Co Method of inhibiting the growth of fungi by applying a complex of organic amine with a completely halogenated acetone
US3933531A (en) * 1972-04-11 1976-01-20 Natsuo Sawa Method of rust-preventing for copper and copper alloy
FR2453157A1 (en) * 1979-04-02 1980-10-31 Fabre Sa Pierre 2-Undecyl imidazole salts - having Gram positive and negative antibacterial activity
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