CN103014716A - Corrosion inhibitor composition for preventing hydrogen sulfide and carbon dioxide corrosion - Google Patents
Corrosion inhibitor composition for preventing hydrogen sulfide and carbon dioxide corrosion Download PDFInfo
- Publication number
- CN103014716A CN103014716A CN2012102816369A CN201210281636A CN103014716A CN 103014716 A CN103014716 A CN 103014716A CN 2012102816369 A CN2012102816369 A CN 2012102816369A CN 201210281636 A CN201210281636 A CN 201210281636A CN 103014716 A CN103014716 A CN 103014716A
- Authority
- CN
- China
- Prior art keywords
- parts
- corrosion
- corrosion inhibitor
- carbon dioxide
- hydrogen sulfide
- 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
Links
Abstract
The invention discloses a corrosion inhibitor composition for preventing hydrogen sulfide and carbon dioxide corrosion, which is characterized by comprising the following components in mass ratio: 1-5 parts of tween, 15-30 parts of ethanol, 20-40 parts of imidazoline derivative, 5-30 parts of alkynol derivative, 1-5 parts of octanol, 2-25 parts of sodium tungstate, and 2-33 parts of water. The corrosion inhibitor composition has the property of preventing hydrogen sulfide and carbon dioxide corrosion suitable for deep oil wells at high temperature, and the corrosion inhibition efficiency on N80 steel is more than 90%.
Description
Technical field
The invention belongs to the inhibiter field, relate to the composite corrosion inhibitor of a kind of anti-H 2 S and carbon dioxide corrosion.
Background technology
Along with going deep into of oil-field development, the metallic corrosion that hydrogen sulfide corrosion and carbonic acid gas form the hybrid corrosion medium increases the weight of gradually, has directly threatened the safety and stability production in oil field.Simultaneously, the hydrogen sulfide that discharges is again highly toxic substance, directly threatens people's healthy and life security.At H
2In S and the simultaneous situation of CO2 corrosive medium, H2S, the CO2 relative content has complicated impact to corrosion.Generally acknowledge that relatively rule is that: H2S is relevant with ratio and the corrosion condition of CO2 content, generally represents its ratio with its dividing potential drop.Ratio PCO when its dividing potential drop
2/ PH
2S<20, corrosion is take H2S as main; 20≤PCO
2/ PH
2S<500, this corrodes with CO
2And H
2The S acting in conjunction is main; PCO
2/ PH
2S 〉=500, in time, corrode take CO2 as main.Simultaneously, the Cl in the water quality
-Ion plays catalyzer in the corrosion process of oil pipe, hinder the iron sulfide film of protectiveness in the formation of steel surface, and Cl
-Can also cross pore or the defective of metal surface sulfurizing iron protective membrane and infiltrate film, make protective membrane that micro-cracking occur, cause pitting.Cl
-In case contact with gold surface, can accelerate the iron ion dissolving, generate the FeCl of facile hydrolysis
3Thereby, accelerated corrosion.
In all multi-control corrosion measures, inhibiter is most economical effective means, selects rational inhibiter.The application specific aim of inhibiter is stronger, and for different corrosive mediums and environment, the inhibiter of use is different, even same medium, when the operating parts such as temperature, pressure, concentration and flow velocity changed, the inhibiter of employing also needed to change.Therefore, should first by indoor compatibleness test, test to select inhibiter in conjunction with field evaluation.Concrete situation for its corrosion, therefore, developing a kind of composite corrosion inhibitor that can effectively control hydrogen sulfide and carbon dioxide mix corrosion or weakening hydrogen sulfide corrosion and carbon dioxide mix corrosion, is very necessary, significant to the healthy of oilfield safety, stably manufactured and people.Inhibiter is a kind of easy of control hydrogen sulfide and carbon dioxide corrosion, economy, effectively one of important substance and method.The inhibition efficiency of inhibiter and steel kind, corrosive environment, the temperature on stratum has close relationship, and the general oil well of western oil field turns well depth and has all surpassed 5000m, and underground environment is complicated, and temperature is higher, and all adopts height to contain Cr, Ni, Mo steel.Employed inhibiter so far can not adapt to the situation in oil field, is difficult to obtain satisfied effect.Therefore, the task of top priority need to be developed a kind of composite inhibiter composition with several functions is controlled hydrogen sulfide corrosion with realization purpose.
Summary of the invention
The objective of the invention is to solve western oil field hydrogen sulfide and carbon dioxide corrosion problem in order to overcome the deficiency of existing inhibiter the work-ing life of Yanchang Oilfield equipment, safety, the stably manufactured in assurance oil field.A kind of anti-H 2 S of suitable oil field deep well and the composite corrosion inhibitor of carbon dioxide corrosion are provided.
To achieve these goals, the present invention's technical scheme of taking of dealing with problems is:
Consider that corrosive environment is the hybrid corrosion environment of hydrogen sulfide and carbonic acid gas, simultaneously, also have chlorion to exist in the corrosive environment, so by adopting tetrahydroglyoxaline to control carbon dioxide corrosion, control hydrogen sulfide corrosion with alkynol, use the sodium wolframate passivating metallic surfaces, raising is to the erosion-resistant effect of chlorion, its concrete scheme is by tween, ethanol, imidazolidine derivatives, propargyl alcohol derivative, octanol, sodium wolframate and water form, and each components in mass portion content range is:
1~5 part of tween,
15~30 parts of ethanol,
20~40 parts of imdazole derivatives,
5~30 parts of propargyl alcohol derivatives,
1~5 part of octanol,
Sodium wolframate 2-25 part,
Water 2-33 part.
The molecular structure of imidazolidine derivatives described above is:
Wherein: R1 and R2 can be identical, also can not be all the alkyl of 1-6 atom, and it derives from the by product of pharmaceutical industry;
The molecular structure of described propargyl alcohol derivative is:
Wherein: R is the alkyl of 1-8 carbon atom, and it derives from following reaction:
Preparation method of the present invention is: after according to proportioning each component directly being joined in the reactor dissolving, stirs, and packing.
During use, be 100mg/L according to concentration, directly join in the environment that uses hardware and get final product.
The present invention compares with existing inhibiter, and the advantage and the beneficial effect that have mainly are:
Have anti-H 2 S in the suitable oil field deep well high temperature and the performance of carbon dioxide corrosion; To N80 steel inhibition efficiency more than 90%.
Embodiment
Embodiment 1
One, the composition of this composite corrosion inhibitor is in mass ratio:
5 parts of tweens,
15 parts of ethanol,
20 parts of imdazole derivatives,
5 parts of propargyl alcohol derivatives,
1 part of octanol,
25 parts of sodium wolframates,
29 parts in water.
Two, the preparation method of this composite corrosion inhibitor is: after each component is directly joined in the reactor dissolving, stirs, and packing.
Three, embodiment effect: N80 steel inhibition efficiency is 90%.
Embodiment 2
One, the composition of this composite corrosion inhibitor is in mass ratio:
1 part of tween,
15 parts of ethanol,
20 parts of imdazole derivatives,
10 parts of propargyl alcohol derivatives,
1 part of octanol,
25 parts of sodium wolframates,
33 parts in water.
Two, the preparation method of this composite corrosion inhibitor is with embodiment 1.
Three, embodiment effect: N80 steel inhibition efficiency is 91%.
Embodiment 3
The mass ratio of its component is:
5 parts of tweens,
25 parts of ethanol,
25 parts of imdazole derivatives,
15 parts of propargyl alcohol derivatives,
3 parts of octanols,
15 parts of sodium wolframates,
12 parts in water.
Two, the preparation method of this composite corrosion inhibitor is with embodiment 1.
Three, embodiment effect: N80 steel inhibition efficiency is 95%.
Embodiment 4
One, the composition of this composite corrosion inhibitor is in mass ratio:
3 parts of tweens,
20 parts of ethanol,
38 parts of imdazole derivatives,
30 parts of propargyl alcohol derivatives,
5 parts of octanols,
2 parts of sodium wolframates,
2 parts in water.
Two, the preparation method of this composite corrosion inhibitor is with embodiment 1.
Three, embodiment effect: N80 steel inhibition efficiency is 92%.
Embodiment 5
One, the composition of this composite corrosion inhibitor is in mass ratio:
4 parts of tweens,
15 parts of ethanol,
30 parts of imdazole derivatives,
30 parts of propargyl alcohol derivatives,
4 parts of octanols,
10 parts of sodium wolframates,
7 parts in water.
Two, the preparation method of this composite corrosion inhibitor is with embodiment 1.
Three, embodiment effect: N80 steel inhibition efficiency is 89%.
Embodiment 6
One, the composition of this composite corrosion inhibitor is in mass ratio:
2 parts of tweens,
24 parts of ethanol,
25 parts of imdazole derivatives,
25 parts of propargyl alcohol derivatives,
3 parts of octanols,
20 parts of sodium wolframates,
26 parts in water.
Two, the preparation method of this composite corrosion inhibitor is with embodiment 1.
Three, embodiment effect: N80 steel inhibition efficiency is 96%.
Embodiment 7
One, the composition of this composite corrosion inhibitor is in mass ratio:
3 parts of tweens,
18 parts of ethanol,
40 parts of imdazole derivatives,
5 parts of propargyl alcohol derivatives,
3 parts of octanols,
25 parts of sodium wolframates,
6 parts in water.
Two, the preparation method of this composite corrosion inhibitor is with embodiment 1.
Three, embodiment effect: N80 steel inhibition efficiency is 97%.
Embodiment 8
One, the composition of this composite corrosion inhibitor is in mass ratio:
2 parts of tweens,
27 parts of ethanol,
35 parts of imdazole derivatives,
28 parts of propargyl alcohol derivatives,
3 parts of octanols,
3 parts of sodium wolframates,
2 parts in water.
Two, the preparation method of this composite corrosion inhibitor is with embodiment 1.
Three, embodiment effect: N80 steel inhibition efficiency is 96%.
Embodiment of the present invention only is used for the explanation technical solution of the present invention, is not limited to the present invention.
Claims (1)
1. the composite corrosion inhibitor of an anti-H 2 S and carbonic acid gas is characterized in that by tween, ethanol, and imidazolidine derivatives, propargyl alcohol derivative, octanol, sodium wolframate and water form, and each components in mass portion content range is:
1~5 part of tween,
15~30 parts of ethanol,
20~40 parts of imdazole derivatives,
5~30 parts of propargyl alcohol derivatives,
1~5 part of octanol,
Sodium wolframate 2-25 part,
Water 2-33 part;
The molecular structure of imidazolidine derivatives described above is:
Wherein: R1 and R2 can be identical, also can not be all the alkyl of 1-6 atom, and it derives from the by product of pharmaceutical industry;
The molecular structure of described propargyl alcohol derivative is:
Wherein: R is the alkyl of 1-8 carbon atom, and it derives from following reaction:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210281636.9A CN103014716B (en) | 2012-08-09 | 2012-08-09 | Corrosion inhibitor composition for preventing hydrogen sulfide and carbon dioxide corrosion |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210281636.9A CN103014716B (en) | 2012-08-09 | 2012-08-09 | Corrosion inhibitor composition for preventing hydrogen sulfide and carbon dioxide corrosion |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103014716A true CN103014716A (en) | 2013-04-03 |
CN103014716B CN103014716B (en) | 2014-09-10 |
Family
ID=47963821
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201210281636.9A Expired - Fee Related CN103014716B (en) | 2012-08-09 | 2012-08-09 | Corrosion inhibitor composition for preventing hydrogen sulfide and carbon dioxide corrosion |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103014716B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110318059A (en) * | 2019-08-09 | 2019-10-11 | 中北大学 | A kind of Compositional type carbon steel pickling corrosion inhibitor and its application |
CN110698956A (en) * | 2019-10-17 | 2020-01-17 | 江苏科技大学 | Carbon dioxide corrosion resistant water-based coating composition and preparation method and application thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4389371A (en) * | 1979-09-14 | 1983-06-21 | Basf Wyandotte Corporation | Process for inhibiting the corrosion of aluminum |
CN101565241A (en) * | 2009-06-04 | 2009-10-28 | 李秀宁 | Non-phosphorus scale and corrosion inhibitor |
CN102061157A (en) * | 2011-01-12 | 2011-05-18 | 中国石油集团川庆钻探工程有限公司 | Gas-liquid double-phase corrosion inhibitor for gas well and preparation method thereof |
WO2011143358A2 (en) * | 2010-05-12 | 2011-11-17 | Jsk Capital Llc | Method for lowering ph using urea sulfate in the presence of corrosion inhibitor |
-
2012
- 2012-08-09 CN CN201210281636.9A patent/CN103014716B/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4389371A (en) * | 1979-09-14 | 1983-06-21 | Basf Wyandotte Corporation | Process for inhibiting the corrosion of aluminum |
CN101565241A (en) * | 2009-06-04 | 2009-10-28 | 李秀宁 | Non-phosphorus scale and corrosion inhibitor |
WO2011143358A2 (en) * | 2010-05-12 | 2011-11-17 | Jsk Capital Llc | Method for lowering ph using urea sulfate in the presence of corrosion inhibitor |
CN102061157A (en) * | 2011-01-12 | 2011-05-18 | 中国石油集团川庆钻探工程有限公司 | Gas-liquid double-phase corrosion inhibitor for gas well and preparation method thereof |
Non-Patent Citations (2)
Title |
---|
王建华 等: ""咪唑啉衍生物缓蚀剂的研制及其性能评价"", 《精细石油化工进展》 * |
高延敏 等: ""油田用水腐蚀和结垢因素与选择缓蚀剂和阻垢剂的关系"", 《全面腐蚀控制》 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110318059A (en) * | 2019-08-09 | 2019-10-11 | 中北大学 | A kind of Compositional type carbon steel pickling corrosion inhibitor and its application |
CN110318059B (en) * | 2019-08-09 | 2021-03-16 | 中北大学 | Compound carbon steel pickling corrosion inhibitor and application thereof |
CN110698956A (en) * | 2019-10-17 | 2020-01-17 | 江苏科技大学 | Carbon dioxide corrosion resistant water-based coating composition and preparation method and application thereof |
Also Published As
Publication number | Publication date |
---|---|
CN103014716B (en) | 2014-09-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Askari et al. | Downhole corrosion inhibitors for oil and gas production–a review | |
Schmitt | Fundamental aspects of CO2 metal loss corrosion. Part II: Influence of different parameters on CO2 corrosion mechanism | |
Ilman | Analysis of internal corrosion in subsea oil pipeline | |
Tavares et al. | Effect of calcium carbonate on low carbon steel corrosion behavior in saline CO2 high pressure environments | |
Liao et al. | Study on corrosion mechanism and the risk of the shale gas gathering pipelines | |
Wang et al. | Inhibitive effects of inhibitors on the galvanic corrosion between N80 carbon steel and 13Cr stainless steel under dynamic supercritical CO2 conditions | |
Dong et al. | Major corrosion influence factors analysis in the production well of CO2 flooding and the optimization of relative anti-corrosion measures | |
US10626319B1 (en) | Methods of inhibiting corrosion with a pyrazine corrosion inhibitor | |
CN101818350A (en) | Anti-oil well metal equipment corrosion inhibitor, preparation method and using method thereof | |
CN104846379A (en) | Preparation method of vegetable oil acid based imidazoline carbon dioxide corrosion inhibitor | |
Paul et al. | Selection of materials for high pressure CO2 transport | |
Crolet | Acid corrosion in wells (CO2, H2S): Metallurgical aspects | |
CN103014715B (en) | Corrosion inhibitor composition for preventing hydrogen sulfide corrosion | |
Aslam et al. | Corrosion inhibitors for sweet (CO2 corrosion) and sour (H2S corrosion) oilfield environments | |
Alaba et al. | Unveiling corrosion behavior of pipeline steels in CO2-containing oilfield produced water: towards combating the corrosion curse | |
Vagapov et al. | Corrosion activity of operating conditions for the steel equipment and pipelines in the plants extracting CO2-containing gases | |
CN103014716B (en) | Corrosion inhibitor composition for preventing hydrogen sulfide and carbon dioxide corrosion | |
Verma | Handbook of science & engineering of green corrosion inhibitors: modern theory, fundamentals & practical applications | |
Ituen et al. | Inhibition of X80 steel corrosion in oilfield acidizing environment using 3-(2-chloro-5, 6-dihydrobenzo [b][1] benzazepin-11-yl)-N, N-dimethylpropan-1-amine and its blends | |
Kimura et al. | High Cr stainless steel OCTG with high strength and superior corrosion resistance | |
Marchebois et al. | Sour service limits of 13% Cr and super 13% Cr stainless steels for OCTG: effect of environmental factors | |
Al-Kharafi et al. | Electrochemical behaviour of low carbon steel in concentrated carbonate chloride brines | |
Liu et al. | Influence factors on stress corrosion cracking of P110 tubing steel under CO2 injection well annulus environment | |
CN104119850A (en) | Corrosion inhibitor used in saline medium, and preparation method thereof | |
Zav'yalov et al. | Chemical, Hydrodynamic, and Metallurgical Factors in West Siberian Oil Pipeline Corrosion Failure. |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140910 Termination date: 20170809 |