CN102660244A - Composite-type oil-gas field corrosion inhibitor - Google Patents

Composite-type oil-gas field corrosion inhibitor Download PDF

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Publication number
CN102660244A
CN102660244A CN2012101539227A CN201210153922A CN102660244A CN 102660244 A CN102660244 A CN 102660244A CN 2012101539227 A CN2012101539227 A CN 2012101539227A CN 201210153922 A CN201210153922 A CN 201210153922A CN 102660244 A CN102660244 A CN 102660244A
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CN
China
Prior art keywords
acid
percent
corrosion
inhibitor
inhibiter
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.)
Pending
Application number
CN2012101539227A
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Chinese (zh)
Inventor
杜磊
张金钟
杨欢
上官昌淮
郭成华
汤晓勇
杜通林
施岱艳
姜放
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China National Petroleum Corp Engineering Design Co Ltd
Original Assignee
China National Petroleum Corp Engineering Design Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by China National Petroleum Corp Engineering Design Co Ltd filed Critical China National Petroleum Corp Engineering Design Co Ltd
Priority to CN2012101539227A priority Critical patent/CN102660244A/en
Priority to PCT/CN2012/075926 priority patent/WO2013170492A1/en
Publication of CN102660244A publication Critical patent/CN102660244A/en
Pending legal-status Critical Current

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Classifications

    • 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
    • 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

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Abstract

The invention relates to a high-efficient composite-type corrosion inhibitor for corrosion resistance of an acid-gas oil-gas field metal material containing carbon dioxide (CO2) and hydrogen sulfide (H2S) and a preparation method thereof. Tall-acid dicyclohexyl amide and triphenylamine oleic acid salt are compounded into a compound, so that the metal corrosion speed can be greatly slowed down under the synergistic action of the tall-acid dicyclohexyl amide and the triphenylamine oleic acid salt. A high-efficient inhibitor is obtained by mixing the following ingredients by weight percent: 15 to 20 percent of the compound, 1 to 3 percent of non-ion surface active agent, 10 to 15 percent of ethylene glycol, 5 to 10 percent of propargyl alcohol and 1 percent of citric acid and balance of water. The composite inhibitor has good solubility and oil dispersion property, the production process is simple, and no environment pollution occurs. The inhibitor has excellent slow-release effect in a corrosion environment and can be used in an acid oil-gas field ground gathering and storage transportation system to prevent the damage of metal materials caused by corrosive gases and to reduce the corrosion loss.

Description

A kind of compound fld inhibiter
Technical field
The present invention relates to a kind of fld inhibiter, be mainly used in oil, gas well production, the anti-corrosion of metal in the pipeline transportation process belongs to field of fine chemical.
Background technology
The continuous development of oil-gas exploration industry is drilled deep formation and is contained H 2S, CO 2, salt solution and composition thereof the stratum increase H gradually 2S and CO 2Gas can cause down-hole oil production, the pitting corrosion of gas equipment or fracture, can not solve the equipment corrosion problem with conventional drilling method and anti-corrosion measure.In medium, add a small amount of inhibiter of people, can significantly reduce Corrosion of Metallic Materials speed, and can keep the physical and mechanical properties of metal constant.Inhibiter has that cost is low, simple to operate, instant effect, can protect integral device, be fit to characteristics such as long-term protection, and the employing inhibiter is undoubtedly one of optimized protection measure of fld equipment.
Traditional fld inhibiter is the organic cpds of non-environment-friendly type, and part also has severe toxicity, such as pyrimidine and shin class etc.As China's oil enterprise improves constantly enterprise-quality, safety, environmental management requirement, is eliminated in succession.
The more inhibiter of present domestic use basically all is an adsorption corrosion inhibitor, like tetrahydroglyoxaline, quaternary ammonium salt and acid amides etc., generally believes that these inhibiter have corrosion inhibition preferably.But tetrahydroglyoxaline and amides inhibiter are water-soluble relatively poor usually, are incompatible with the fld chemicaladditives, very easily produce deposited phenomenon, have a strong impact on the result of use of various medicaments.
Summary of the invention
Technical problem to be solved by this invention provides the good fld inhibiter of a kind of compatibleness.
Except as otherwise noted, the per-cent that occurs among this paper all is the quality percentage composition.
Main points of the present invention are: unite the host as inhibiter with appropriate youngster's acid two Cyclohexamides and triphenylamine oleate.The concrete prescription of fld inhibiter of the present invention is:
Acyl group in appropriate youngster's acid two Cyclohexamides has increased amino cloud density; Phenyl ring in the triphenylamine oleate and amino conjugation have increased the cloud density of N atom, make that the unoccupied orbital on they and the iron atom forms co-ordination bond; Adsorbed close is on the surface of iron; The long-chain hydrophobic alkyl of the other end can effectively stop the admission velocity of water and etching reagent, and the two synergy delays rate of metal corrosion greatly.
The preparation method of appropriate youngster acid two Cyclohexamides in the above-mentioned prescription can for:
In the good there-necked flask of drying, add appropriate youngster's acid of 0.1mol and 0.15mol sulfur oxychloride, nitrogen protection, reflux half a hour in water-bath, reaction system keeps dry.After having the flue gas generation, do not add 0.12mol dicyclohexyl amine and 20ml pyridine, reflux 4 ~ 5 hours.With ice bath reactant is cooled off and stirring.Take out throw out, use a small amount of cold water flush, drying is utilized the pyridine dissolving to carry out recrystallization and is obtained white powder, is appropriate youngster's acid two Cyclohexamides.
The preparation method of the described triphenylamine oleate in the above-mentioned prescription can for:
Use mol ratio to add flask, fully stir down at 70 ℃ as oleic acid and the triphenylamine of 1:1, to dissolving fully, constant temperature 3 hours, cooling is after recrystallization obtains the triphenylamine oleate.
The preparation method of fld inhibiter of the present invention is: be dissolved in the water Hydrocerol A earlier, add hexylene glycol, propiolic alcohol and nonionogenic tenside more respectively, after fully stirring, add appropriate youngster's acid two Cyclohexamides and triphenylamine oleate, stirring gets final product.
Fld inhibiter of the present invention is used for fld and contains CO 2And H 2The oil well of S, gas well, and the ducted anti-corrosion of metal of surface gathering and transferring.
Inhibitor agent of the present invention is used for acid and peracidity fld collection is defeated and storing and transporting system.
Fld inhibiter of the present invention has good dispersiveness, reaches one-level with the compatibility of acid fluid system, and inhibition efficiency can reach 95%.Have advantages such as compatibleness is good, practicality is wide, in actual use, more can bring into play good corrosion prevention effect, also do not influence the use properties of other chemical agents simultaneously.
Embodiment
Embodiment 1
Inhibiter Example formulations such as following table (mass percent %):
Table one formula test
Recipe: be dissolved in the water Hydrocerol A earlier, add hexylene glycol, propiolic alcohol and nonionogenic tenside more respectively, fully stir, add appropriate youngster's acid two Cyclohexamides and triphenylamine oleate again, stirring at last gets final product.
Embodiment 2
Contact angle is measured
Contact angle is meant that the tangent line of the liquid-vapo(u)r interface of doing in gas, liquid, solid three joining places passes the angle between liquid and the solid-liquid boundary line, is measuring of wetness degree, is to weigh liquid combines tightness degree at solid surface important indicator.Utilize Kruss DSA20 type contact angle measurement to record the contact angle such as the table two of above-mentioned four kinds of corrosion inhibitor formulas and steel surface; This shows that there is good wellability on this inhibiter and steel surface; Contact closely can effectively stop corrosive fluid to contact with carbon steel, plays good corrosion inhibition.
Table two contact angle is measured
The test sequence number Contact angle (degree)
Prescription 1 15.5
Prescription 2 15.1
Prescription 3 14.9
Prescription 4 15.4
Embodiment 3
Inhibition efficiency is measured
According to SY 5405-1996 " acidifying is with inhibiter method for testing performance and evaluation index ", specify the corrosion mitigating effect of novel corrosion inhibitor of the present invention through test simulation, see table three.Concrete steps:
(a) material for test is N-80, is of a size of 50 * 10 * 3mm.Test temperature is 140 ℃, and pressure is 16MPa, and test period is 4 hours.
(b) acid solution be hydrochloric be 15%, or mud acid is 15% solution (with reference to the table 3 among the SY 5405-1996 " acidifying is with inhibiter method for testing performance and evaluation index ").Add novel corrosion inhibitor in the instance 1 to acid solution, the inhibiter consumption is 2%~3% of an acid solution.
(c) test is preceding with 400 #Abrasive paper for metallograph is polished to light to test piece one by one, uses the acetone surface again, removes degreasing.
(d) after drying is weighed, soak 4 hours (doing blank simultaneously with the acid solution that does not add inhibiter) in the acid solution of test piece adding homothermic adding inhibiter, weigh again.
(e) calculate weightlessness, calculate erosion rate and corrosion rate by following formula (1) and formula (2).
Erosion rate is calculated formula:
v = 10 6 × Δm A × Δt - - - ( 1 )
In the formula: v ... Erosion rate, g/ (m 2H);
△ t ... Reaction times, h;
△ m ... The test piece corrosion weight loss, g;
A ... The test piece surface-area, mm 2
Corrosion inhibition rate calculation formula formula is:
η = v 0 - v v 0 - - - ( 2 )
In the formula: η ... Corrosion inhibition rate, %;
v 0The erosion rate that does not add inhibiter, g/ (m 2H);
V ... Be added with the erosion rate of inhibiter, g/ (m 2H).
(f) concrete acid solution is formed and experimental data calculates inhibition speed and inhibition efficiency such as table three.
Table three corrosion efficient

Claims (2)

1. a fld inhibiter is characterized in that, its composition and mass percent are:
Appropriate youngster's acid two Cyclohexamide 5%-20%
Triphenylamine oleate 10%-30%
Nonionogenic tenside 1%-3%
Hexylene glycol 10%-15%
Propiolic alcohol 5%-10%
Hydrocerol A 1%-3%
Water surplus.
2. the preparation method of a fld inhibiter is characterized in that, is dissolved in the water Hydrocerol A earlier; Add hexylene glycol, propiolic alcohol and nonionogenic tenside more respectively; After fully stirring, add appropriate youngster's acid two Cyclohexamides and triphenylamine oleate, stir.
CN2012101539227A 2012-05-17 2012-05-17 Composite-type oil-gas field corrosion inhibitor Pending CN102660244A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN2012101539227A CN102660244A (en) 2012-05-17 2012-05-17 Composite-type oil-gas field corrosion inhibitor
PCT/CN2012/075926 WO2013170492A1 (en) 2012-05-17 2012-05-23 Corrosion inhibitor for composite oil-gas field

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012101539227A CN102660244A (en) 2012-05-17 2012-05-17 Composite-type oil-gas field corrosion inhibitor

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CN102660244A true CN102660244A (en) 2012-09-12

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WO (1) WO2013170492A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103882437A (en) * 2014-04-01 2014-06-25 马杨洋 Corrosion inhibitor for oil-gas gathering and transportation pipeline and preparation method thereof

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114481138B (en) * 2022-01-28 2023-12-01 东北石油大学 Metal corrosion inhibitor for oil field and preparation method thereof

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6063334A (en) * 1998-03-06 2000-05-16 Champion Technologies, Inc. Sulfur based corrosion inhibitor
US6695897B1 (en) * 2002-12-26 2004-02-24 Cortec Corporation Corrosion resistant system for performance drilling fluids utilizing formate brine
US20050148478A1 (en) * 2004-01-07 2005-07-07 Nubar Ozbalik Power transmission fluids with enhanced anti-shudder characteristics
CN1769529A (en) * 2004-11-05 2006-05-10 姚凯 Oil well acidification inhibitor and its preparation method
CN102168272B (en) * 2011-03-22 2012-12-26 中国石油集团工程设计有限责任公司 Corrosion inhibitor for sour oil and gas fields

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103882437A (en) * 2014-04-01 2014-06-25 马杨洋 Corrosion inhibitor for oil-gas gathering and transportation pipeline and preparation method thereof
CN103882437B (en) * 2014-04-01 2015-12-30 马杨洋 Oil-gas gathering and transferring pipeline inhibiter and preparation method thereof

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Application publication date: 20120912