USH751H - Method of inhibiting acid corrosion of ferrous metals - Google Patents
Method of inhibiting acid corrosion of ferrous metals Download PDFInfo
- Publication number
- USH751H USH751H US07/204,839 US20483988A USH751H US H751 H USH751 H US H751H US 20483988 A US20483988 A US 20483988A US H751 H USH751 H US H751H
- Authority
- US
- United States
- Prior art keywords
- aryl
- acid
- halogen
- substituted
- quaternary compound
- 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.)
- Abandoned
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23F—NON-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
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/04—Inhibiting 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
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/54—Compositions for in situ inhibition of corrosion in boreholes or wells
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/62—Compositions for forming crevices or fractures
- C09K8/72—Eroding chemicals, e.g. acids
- C09K8/74—Eroding chemicals, e.g. acids combined with additives added for specific purposes
Definitions
- This invention relates generally to acid corrosion inhibitors and in particular to corrosion inhibitors useful in oil field treating operations.
- the invention relates to a method of using a substituted quaternary compound as an acid corrosion inhibitor.
- the invention relates to the use of an aqueous acid solution containing a substituted quaternary compound.
- an aqueous acid solution is injected down the well into the formation to dissolve formation materials and/or other materials deposited in the wellbore thereby improving permeability of the formation and its production.
- the acid treatment may be carried out under matrix injection rates or fracturing rates.
- a serious problem associated with acidizing formations is the high corrosivity of the acid solution on surface and subsurface metal equipment.
- the acid normally HCl or mud acid (HCl-HF mixture)
- HCl-HF mixture is highly corrosive to ferrous metals. Accordingly, the acid treatment almost always involves the use of corrosion inhibitors.
- Corrosion inhibitors used in the past in acid treatment of wells include various acetylenic alcohols, fluorinated surfactants, quaternary derivatives of heterocyclic nitrogen bases and halomethylated aromatic compounds, formamides and surface active agents, alone or in combination with other materials. Examples of these prior art corrosion inhibitors are disclosed in U.S. Pat. Nos. 3,658,720 and 4,028,268.
- the method of the present invention involves the steps of contacting a ferrous metal, which is susceptible to acid corrosion, with an effective amount of a corrosion inhibitor comprising a quaternary compound prepared by reacting a tertiary aromatic heterocyclic amine with a (halo-substituted-aryl) alkyl halide wherein the alkyl group contains from 1 to 3 carbon atoms and the halogen substitution of the (halo-substituted-aryl) group is on the aromatic ring.
- the preferred halides include halobenzyl halides and (halo-substituted-phenyl) alkyl halides.
- the preferred method of practicing the present invention is to prepare a corrosion inhibitor formulation package including the corrosion inhibitor quaternary compound with or without other compounds and inhibitors, and to subsequently use this corrosion inhibitor formulation package to prepare an inhibited acid solution in one step.
- the corrosion inhibitor preferably has the following formula: ##STR1## wherein ARYL is a heterocyclic aromatic ring or rings; N + is a positively charged nitrogen atom and is part of ARYL; ARYL is an aromatic ring or rings; R is an alkyl group containing from 1 to 3 carbon atoms and connects N + to ARYL'; X is a halogen; Y is a halogen substituted on ARYL'; and Z is hydrogen or a halogen substituted on ARYL'.
- the preferred method for carrying out the present invention involves incorporating a small but effective amount of the quaternary corrosion inhibitor in an aqueous acid solution for treatment of subterranean formations.
- the aqueous acid solution includes solutions of hydrochloric acid (HCl), mud acid (a mixture of hydrochloric acid and hydrofluoric acid), acetic acid and formic acid.
- hydrochloric acid HCl
- mud acid a mixture of hydrochloric acid and hydrofluoric acid
- acetic acid formic acid.
- sulfuric acid is not normally used in the petroleum industry, it is used in pickling operations and therefore is included herein. All of these acids are highly corrosive to ferrous metals and therefore require inhibition.
- the concentration of the corrosion inhibitor should be sufficiently high to inhibit corrosion of the ferrous metals and normally will range from 0.01 to 10 percent (preferably 0.05 to 3.0 %) by volume based on the combined volume of the inhibitor and acid solution.
- the inhibitor concentration in a particular treatment will depend on several factors including acid type and concentration, temperature, exposure time, and the presence of other additives. It is important that the inhibitor be added to the acid as early as possible to protect storage, pumping and handling equipment, as well as tubular goods in the well.
- the quaternary compound is the reaction product of a tertiary aromatic heterocyclic amine and a (halo substituted aryl) alkyl halide, having the following formula. ##STR2## wherein ARYL is a heterocyclic aromatic ring or rings; N + is a positively charged nitrogen atom and is part of AHYL; ARYL' is an aromatic ring or rings; and R is an alkyl group containing from 1 to 3 carbon atoms and connects N + to ARYL'; X is a halogen; Y is a halogen substituted on ARYL'; and Z is a halogen or hydrogen substituted on ARYL'.
- the preferred quaternary compound is selected from the group consisting of: ##STR3## wherein R is an alkyl group containing from 1 to 3 carbon atoms; X and Y are halogens; and Z is a halogen or hydrogen.
- the preferred tertiary aromatic heterocyclic amines include quinoline, quinaldine, isoquinoline, pyridine, acridine, phenanthridine, and mixtures and substitutions of these.
- Certain industrially available mixtures of amines are particularly suited for this role including coal tar bases, which contain mixtures of quinoline, isoquinoline, substituted quinolines and isoquinolines, quinaldine and other unreactive materials such as indole.
- Industrially available mixtures of alkyl pyridines are also quite suitable for this role.
- the preferred (halo-substituted-aryl) alkyl halides are (halobenzyl) halides or halo substituted halomethyl naphthalenes having the following formulas: ##STR4## where X and Y are halogens and Z is hydrogen H, or a halogen.
- Chlorine is the most preferred halogen substituent.
- Z be the same as Y.
- the preferred (halo-substituted-aryl) alkyl halides are the (halo substituted) or (dihalo substituted) benzyl halides.
- Specific benzyl halides useable include chlorobenzyl chloride, fluorobenzyl chloride, bromobenzyl chloride, iodobenzyl chloride and the various isomeric dichlorobenzyl chlorides (also known as trichlorotoluene, in which of the chlorine atoms are on the aromatic ring and one of the chlorine atoms is on the methylene carbon), with the halobenzyl chlorides being preferred, in particular, the chlorobenzyl chlorides.
- the chlorobenzyl chlorides are relatively low in cost and exhibit excellent inhibition properties.
- the tertiary aromatic amine compound is reacted with the (halo-substituted-aryl) alkyl halide in proper stoichiometric proportions and at the reaction conditions to achieve substantial formation of the quaternary compound wherein the halogen on the aromatic ring of the (halo-substituted-aryl) alkyl halide does not enter into the reaction and remains intact on the aromatic ring. It is believed that the presence of this halogen contributes to the corrosion inhibition properties of the quaternary compound.
- the reaction of a tertiary heterocyclic amine with a halobenzyl halide may be described as follows.
- the selected tertiary heterocyclic amine and the selected halobenzyl halide are charged to a reactor on an equal mole to mole basis.
- a small amount of solvent e.g. 10% of charge
- the reaction mixture is heated with agitation and the temperature is elevated to between about 120° to 140° C.
- the reaction is continued for three to seven hours depending on the specific reactants selected.
- additional solvent may be added to produce a solution of a quaternary compound in liquid form. Sixty percent (60%) in isopropanol has been found to be a convenient concentration.
- the corrosion inhibitor, dissolved or dispersed in the solvent may be introduced into the aqueous acid at a concentration to provide protection of ferrous metals against acid corrosion.
- additives which may be included in the aqueous acid package are acetylenic alcohol, surfactants, hydrocarbons, formic acid derivatives (e.g. formamide), other quaternary compounds, etc.
- additives for well stimulation and workover treatments may be included in the package. These include compounds such as mutual solvents (e.g. ethylene glycol monobutyl ether) and complex surfactant formulations designed to prevent formation of emulsions. These additives as well as many others are routinely used in acid corrosion formulation packages.
- the preferred corrosion inhibitor additive components for introduction into an aqueous acid include the following:
- acetylenic alcohols improves effect of quaternary compound
- surfactant water soluble; dispersant; contributes to pitting control to reduce corrosion rates
- hydrocarbon liquid oil wet metal surface (e.g. heavy aromatic naphtha, pine oil, mineral oil and C 14 -C 20 fatty acids such as tall oil fatty acid.
- oil wet metal surface e.g. heavy aromatic naphtha, pine oil, mineral oil and C 14 -C 20 fatty acids such as tall oil fatty acid.
- the corrosion inhibitor may be used alone but preferably is used in a package (containing one or more of the the above additives), which is especially formulated for optimum performance.
- the entire package may be added to the acid solution.
- the preferred corrosion inhibitor packages are as follows:
- the corrosion inhibitor package may be added to the acid solution and transported to the well site.
- the aqueous acid solution with the corrosion inhibitor package may then be pumped into the well using conventional techniques and equipment.
- Samples 1, 18, and 27 represent prior art corrosion inhibitors.
- Samples 1 through 27 were prepared as a 60% concentrated solution in isopropyl alcohol and tested in an acid corrosion testing autoclave. Certain test samples included corrosion inhibitor and additives and other test samples included only the corrosion inhibitor. The corrosion inhibitor sample and other additives, if used, were added to a 15% HCl acid solution at a concentration as indicated in Table II based on the total weight of the final solution.
Abstract
A method for inhibiting acid corrosion of metal well equipment which comprises introducing into an aqueous acid solution an inhibiting amount of a quaternary compound prepared by reacting a tertiary aromatic heterocyclic amine with a (halo-substituted-aryl) alkyl halide, and contacting the well equipment with the inhibited aqueous acid solution.
Description
This invention relates generally to acid corrosion inhibitors and in particular to corrosion inhibitors useful in oil field treating operations. In one aspect the invention relates to a method of using a substituted quaternary compound as an acid corrosion inhibitor. In another aspect the invention relates to the use of an aqueous acid solution containing a substituted quaternary compound.
In the acid treatment of subterranean formations penetrated by a wellbore, an aqueous acid solution is injected down the well into the formation to dissolve formation materials and/or other materials deposited in the wellbore thereby improving permeability of the formation and its production. The acid treatment may be carried out under matrix injection rates or fracturing rates.
A serious problem associated with acidizing formations is the high corrosivity of the acid solution on surface and subsurface metal equipment. The acid, normally HCl or mud acid (HCl-HF mixture), is highly corrosive to ferrous metals. Accordingly, the acid treatment almost always involves the use of corrosion inhibitors.
Corrosion inhibitors used in the past in acid treatment of wells include various acetylenic alcohols, fluorinated surfactants, quaternary derivatives of heterocyclic nitrogen bases and halomethylated aromatic compounds, formamides and surface active agents, alone or in combination with other materials. Examples of these prior art corrosion inhibitors are disclosed in U.S. Pat. Nos. 3,658,720 and 4,028,268.
The method of the present invention involves the steps of contacting a ferrous metal, which is susceptible to acid corrosion, with an effective amount of a corrosion inhibitor comprising a quaternary compound prepared by reacting a tertiary aromatic heterocyclic amine with a (halo-substituted-aryl) alkyl halide wherein the alkyl group contains from 1 to 3 carbon atoms and the halogen substitution of the (halo-substituted-aryl) group is on the aromatic ring. The preferred halides include halobenzyl halides and (halo-substituted-phenyl) alkyl halides.
The preferred method of practicing the present invention is to prepare a corrosion inhibitor formulation package including the corrosion inhibitor quaternary compound with or without other compounds and inhibitors, and to subsequently use this corrosion inhibitor formulation package to prepare an inhibited acid solution in one step.
The corrosion inhibitor preferably has the following formula: ##STR1## wherein ARYL is a heterocyclic aromatic ring or rings; N+ is a positively charged nitrogen atom and is part of ARYL; ARYL is an aromatic ring or rings; R is an alkyl group containing from 1 to 3 carbon atoms and connects N+ to ARYL'; X is a halogen; Y is a halogen substituted on ARYL'; and Z is hydrogen or a halogen substituted on ARYL'.
The preferred method for carrying out the present invention involves incorporating a small but effective amount of the quaternary corrosion inhibitor in an aqueous acid solution for treatment of subterranean formations. The aqueous acid solution includes solutions of hydrochloric acid (HCl), mud acid (a mixture of hydrochloric acid and hydrofluoric acid), acetic acid and formic acid. Although sulfuric acid is not normally used in the petroleum industry, it is used in pickling operations and therefore is included herein. All of these acids are highly corrosive to ferrous metals and therefore require inhibition. The concentration of the corrosion inhibitor should be sufficiently high to inhibit corrosion of the ferrous metals and normally will range from 0.01 to 10 percent (preferably 0.05 to 3.0 %) by volume based on the combined volume of the inhibitor and acid solution. The inhibitor concentration in a particular treatment will depend on several factors including acid type and concentration, temperature, exposure time, and the presence of other additives. It is important that the inhibitor be added to the acid as early as possible to protect storage, pumping and handling equipment, as well as tubular goods in the well.
The quaternary compound, as mentioned above, is the reaction product of a tertiary aromatic heterocyclic amine and a (halo substituted aryl) alkyl halide, having the following formula. ##STR2## wherein ARYL is a heterocyclic aromatic ring or rings; N+ is a positively charged nitrogen atom and is part of AHYL; ARYL' is an aromatic ring or rings; and R is an alkyl group containing from 1 to 3 carbon atoms and connects N+ to ARYL'; X is a halogen; Y is a halogen substituted on ARYL'; and Z is a halogen or hydrogen substituted on ARYL'.
The preferred quaternary compound is selected from the group consisting of: ##STR3## wherein R is an alkyl group containing from 1 to 3 carbon atoms; X and Y are halogens; and Z is a halogen or hydrogen.
The preferred tertiary aromatic heterocyclic amines include quinoline, quinaldine, isoquinoline, pyridine, acridine, phenanthridine, and mixtures and substitutions of these. Certain industrially available mixtures of amines are particularly suited for this role including coal tar bases, which contain mixtures of quinoline, isoquinoline, substituted quinolines and isoquinolines, quinaldine and other unreactive materials such as indole. Industrially available mixtures of alkyl pyridines are also quite suitable for this role.
The preferred (halo-substituted-aryl) alkyl halides are (halobenzyl) halides or halo substituted halomethyl naphthalenes having the following formulas: ##STR4## where X and Y are halogens and Z is hydrogen H, or a halogen.
Chlorine is the most preferred halogen substituent. In the embodiment which employs di halogen substitution on the aromatic ring, it is preferred that Z be the same as Y.
The preferred (halo-substituted-aryl) alkyl halides are the (halo substituted) or (dihalo substituted) benzyl halides. Specific benzyl halides useable include chlorobenzyl chloride, fluorobenzyl chloride, bromobenzyl chloride, iodobenzyl chloride and the various isomeric dichlorobenzyl chlorides (also known as trichlorotoluene, in which of the chlorine atoms are on the aromatic ring and one of the chlorine atoms is on the methylene carbon), with the halobenzyl chlorides being preferred, in particular, the chlorobenzyl chlorides. The chlorobenzyl chlorides are relatively low in cost and exhibit excellent inhibition properties.
In preparing the corrosion inhibitor, the tertiary aromatic amine compound is reacted with the (halo-substituted-aryl) alkyl halide in proper stoichiometric proportions and at the reaction conditions to achieve substantial formation of the quaternary compound wherein the halogen on the aromatic ring of the (halo-substituted-aryl) alkyl halide does not enter into the reaction and remains intact on the aromatic ring. It is believed that the presence of this halogen contributes to the corrosion inhibition properties of the quaternary compound. While not fully understood, it is believed that the presence of the halogen on the aromatic ring exerts an electron withdrawing influence on the aromatic ring and therefore contributes to formation of a more dense packing of molecules on the metal surface. This dense packing results in improved protection from the acid. The degree of protection is particularly surprising in view of the relatively small size the ring halogen atom in comparison to the quaternary compound. The corrosion inhibitor prepared from the preferred (halo substituted) benzyl chlorides offer advantages over several corrosion inhibitors because they can be prepared from readily available starting materials.
The reaction of a tertiary heterocyclic amine with a halobenzyl halide may be described as follows. The selected tertiary heterocyclic amine and the selected halobenzyl halide are charged to a reactor on an equal mole to mole basis. A small amount of solvent (e.g. 10% of charge) is then added to the reactor. The reaction mixture is heated with agitation and the temperature is elevated to between about 120° to 140° C. The reaction is continued for three to seven hours depending on the specific reactants selected. At the end of the reaction, additional solvent may be added to produce a solution of a quaternary compound in liquid form. Sixty percent (60%) in isopropanol has been found to be a convenient concentration.
The corrosion inhibitor, dissolved or dispersed in the solvent may be introduced into the aqueous acid at a concentration to provide protection of ferrous metals against acid corrosion.
Other additives which may be included in the aqueous acid package are acetylenic alcohol, surfactants, hydrocarbons, formic acid derivatives (e.g. formamide), other quaternary compounds, etc. In addition, other additives for well stimulation and workover treatments may be included in the package. These include compounds such as mutual solvents (e.g. ethylene glycol monobutyl ether) and complex surfactant formulations designed to prevent formation of emulsions. These additives as well as many others are routinely used in acid corrosion formulation packages.
The preferred corrosion inhibitor additive components for introduction into an aqueous acid include the following:
______________________________________
Broad Range
Preferred Range
(Vol % of Acid
(Vol % of Acid
Soln.) Soln.)
______________________________________
Corrosion inhibitor of
0.01-4.0 0.1-2.0
the present invention
Acetylenic Alcohols
0-4.0 0.1-2.0
Hydrocarbon liquid
0-1.0 0-0.5
Surfactant 0-1.0 0-0.5
Formamide or formic acid
0-20.0 0-10.0
______________________________________
The purpose of these additives are as follows:
acetylenic alcohols: improves effect of quaternary compound
surfactant: water soluble; dispersant; contributes to pitting control to reduce corrosion rates
formamide or formic acid: inhibitor intensifier
hydrocarbon liquid: oil wet metal surface (e.g. heavy aromatic naphtha, pine oil, mineral oil and C14 -C20 fatty acids such as tall oil fatty acid.
The corrosion inhibitor may be used alone but preferably is used in a package (containing one or more of the the above additives), which is especially formulated for optimum performance. The entire package may be added to the acid solution. The preferred corrosion inhibitor packages are as follows:
______________________________________
Broad Range Preferred Range
(wt % of Package)
(wt % of Package)
______________________________________
Corrosion inhibitor of
2-100 5-50
the present invention
Acetylenic Alcohols
0-80 5-25
Hydrocarbon liquid
0-30 5-20
Surfactant 0-20 1-10
Formamide or formic
0-90 10-50
acid
______________________________________
In connection with well treating operations, the corrosion inhibitor package may be added to the acid solution and transported to the well site. The aqueous acid solution with the corrosion inhibitor package may then be pumped into the well using conventional techniques and equipment.
The samples of the corrosion inhibitors listed in Table I were prepared in isopropyl alcohol by the method described above.
TABLE I
______________________________________
Quaternary Compounds
SAMPLE HETEROCYCLIC QUATERNIZATION
NO. AMINE AGENT
______________________________________
1 Coal Tar Bases Benzyl Chloride
2 Coal Tar Bases 2-Chlorobenzyl Chloride
3 Coal Tar Bases 3-Chlorobenzyl Chloride
4 Coal Tar Bases 4-Chlorobenzyl Chloride
5 Coal Tar Bases 2-Fluorobenzyl Chloride
6 Coal Tar Bases 3-Fluorobenzyl Chloride
7 Coal Tar Bases 4-Fluorobenzyl Chloride
8 Coal Tar Bases 2-Bromobenzyl Bromide
9 Coal Tar Bases 3-Bromobenzyl Bromide
10 Coal Tar Bases 4-Bromobenzyl Bromide
11 Coal Tar Bases a-2,6-Trichlorotoluene
12 Coal Tar Bases a-2,4-Trichlorotoluene
13 Coal Tar Bases a-3,4-Trichlorotoluene
14 Isoquinoline 2-Chlorobenzyl Chloride
15 Quinaldine 2-Chlorobenzyl Chloride
16 Quinoline 2-Chlorobenzyl Chloride
17 2,3-Cyclohexenopyridine
2-Chlorobenzyl Chloride
18 2,3-Cyclohexenopyridine
Benzyl Chloride
19 6-Methylquinoline
2-Chlorobenzyl Chloride
20 4-Methylquinoline
2-Chlorobenzyl ChIoride
21 Acridine 2-Chlorobenzyl Chloride
22 Phenanthridine 2-Chlorobenzyl Chloride
23 Coal Tar Bases 2-Iodobenzyl Chloride
24 Coal Tar Bases Chloromethyl Chloronaph-
thalene
25 4-Chloroquinoline
2-Chlorobenzyl Chloride
26 4-Ethylpyridine 2-Chlorobenzyl Chloride
27 4-Ethylpyridine Benzyl Chloride
______________________________________
Note that Samples 1, 18, and 27 represent prior art corrosion inhibitors.
Samples 1 through 27 were prepared as a 60% concentrated solution in isopropyl alcohol and tested in an acid corrosion testing autoclave. Certain test samples included corrosion inhibitor and additives and other test samples included only the corrosion inhibitor. The corrosion inhibitor sample and other additives, if used, were added to a 15% HCl acid solution at a concentration as indicated in Table II based on the total weight of the final solution. The additive, identified as Formula A, had the following composition
______________________________________
wt %
______________________________________
Formula A
Acetylenic Alcohol
14.6
Surfactant 7.4
Hydrocarbon Liquid
19.4
Formamide 39.6
Solvent (alcohol) 19.0
TOTAL 100.0
______________________________________
Metal coupons made from schedule N80 steel tubing were exposed to the inhibited acid mixture. After the test exposure, the coupons were cleaned, dried, weighed and visually evaluated for corrosion effects. The corrosion rate (in pounds of steel lost per square foot of area) was calculated from the weight loss data.
The HCl solution with additives thus prepared were tested under various test conditions at various treating rates as shown in Table II.
TABLE II
__________________________________________________________________________
TEST CONDITIONS
SAMPLE ADDITIVE TEMP.
PRESS.
TIME
TESTS
wt % ADDITIVE
wt % ACID °F.
Psig Hrs.
__________________________________________________________________________
Series
A 0.9 Formula A
2.1 15% HCl
325 4000 6
B 0.9 Formula A
2.1 15% HCl
300 4000 6
Series
C 1.0 -- -- 15% HCl
180 atm 6
D 2.0 -- -- 15% HCl
300 4000 4
E 2.0 Formic acid
2.0 15% HCl
300 4000 4
F 2.0 Surfactant.sup.1
1.0 15% HCl
300 4000 4
G 2.0 PA.sup.2
2.0 15% HCl
300 4000 4
H 2.0 KI 1.0.sup.3
15% HCl
300 4000 4
I 2.0 Cu.sub.2 I.sub.2
1.03 15% HCl
300 4000 4
__________________________________________________________________________
.sup.1 ethoxylated nonyl phenol (10 moles EO)
.sup.2 Propargyl alcohol
.sup.3 1 gram/100 ml
The corrosion coupon test data are presented in Tables III through XI.
TABLE III
______________________________________
Series A
CORROSION
SAMPLE RATE
NO. (LB/SQ FT)
______________________________________
1* .2896
2 .1577
3 .1822
4 .2167
5 .2858
6 .2168
7 .3298
8 .2840
9 .2803
10 .2126
11 .1480
12 .2095
13 .1939
______________________________________
*Prior art corrosion inhibitor
TABLE IV
______________________________________
Series B
CORROSION
SAMPLE RATE
NO. (LB/SQ FT)
______________________________________
1* .0798
2 .0349
3 .0572
4 .0440
5 .0552
6 .0378
7 .0806
10 .0381
______________________________________
*Prior art corrosion inhibitor
TABLE V
______________________________________
Series C
CORROSION
SAMPLE RATE
NO. (LB/SQ FT)
______________________________________
1* .0935
2 .0559
3 .0143
4 .0192
5 .1106
6 .0690
7 .0659
8 .1281
9 .1146
10 .0788
11 .1081
13 .0150
14 .2550
15 .0951
16 .0192
17 .3077
18* .3648
19 .0168
20 .0645
21 .5980
22 .0575
23 .0583
24 .0657
25 .3731
26 .2933
27* .4038
28 .3648
______________________________________
*Prior art corrosion inhibitor
TABLE VI
______________________________________
Series D
CORROSION
SAMPLE RATE
NO. (LB/SQ FT)
______________________________________
1* .3261
2 .2139
3 .1696
4 .1530
5 .3801
6 .3689
7 .3839
8 .4425
9 .3492
10 .3716
11 .2731
13 .2603
______________________________________
*Prior art corrosion inhibitor
TABLE VII
______________________________________
Series E
CORROSION
SAMPLE RATE
NO. (LB/SQ FT)
______________________________________
1* .0479
2 .0255
3 .0301
4 .0254
______________________________________
*Prior art corrosion inhibitor
TABLE VIII
______________________________________
Series F
CORROSION
SAMPLE RATE
NO. (LB/SQ FT)
______________________________________
1* .7441
2 .6404
3 .2309
4 .2098
______________________________________
*Prior art corrosion inhibitor
TABLE IX
______________________________________
Series G
CORROSION
SAMPLE RATE
NO. (LB/SQ FT)
______________________________________
1* .1720
2 .0765
3 .0771
4 .0805
______________________________________
*Prior art corrosion inhibitor
TABLE X
______________________________________
Series H
CORROSION
SAMPLE RATE
NO. (LB/SQ FT)
______________________________________
1* .1575
2 .2046
3 .1476
4 .1024
______________________________________
*Prior art corrosion inhibitor
TABLE XI
______________________________________
Series I
CORROSION
SAMPLE RATE
NO. (LB/SQ FT)
______________________________________
1* .0335
2 .0276
3 .0300
4 .0284
______________________________________
*Prior art corrosion inhibitor
The above corrosion tests show that the corrosion inhibitor of the present invention is quite effective alone or with additives in providing protection over a wide range of test conditions.
Claims (21)
1. A method of inhibiting corrosion of ferrous metals which comprises treating a system wherein metals are susceptible to corrosion with a corrosion inhibiting amount of a quaternary compound prepared by reacting a tertiary aromatic heterocyclic amine with a (halo-substituted-aryl) alkyl halide wherein the halogen substitution on the aromatic ring of the (halo-substituted -aryl) alkyl halide does not enter into the reaction and remains intact on said aromatic ring, and the alkyl group contains from 1 to 3 carbon atoms.
2. The method of claim 1 wherein the heterocyclic amine is selected from the group consisting of quinoline, isoquinoline, quinaldine, pyridine, acridine, phenanthridine, and coal tar bases, with or without substituents, and mixtures of the foregoing.
3. The method of claim 1, wherein the quaternary compound has the formula of: ##STR5## wherein ARYL is a heterocyclic ring or rings; N+ is a positively charged nitrogen atom and is part of ARYL; ARYL' is an aromatic ring or rings; R is an alkyl group containing from 1 to 3 carbon atoms and connects N+ to ARYL'; X is a halogen; Y is a halogen substituted on ARYL'; and Z is a halogen or hydrogen substituted on ARYL'.
4. The method of claim 1 wherein the quaternary compound has a formula selected from the group consisting of ##STR6## wherein R is an alkyl group containing from 1 to 3 carbon atoms; X and Y are halogens; and Z is a halogen or hydrogen.
5. The method of claim 1 wherein the (halo-substituted-aryl) alkyl halide is halobenzyl halide.
6. A method of acidizing a subterranean formation penetrated by a well having pipe extending from the surface to said formation, which comprises injecting through the pipe and into said formation an aqueous acid solution having dissolved or dispersed therein an acid inhibiting amount of a quaternary compound prepared by the reaction of a tertiary heterocyclic amine with a halogen substituted benzyl halide wherein the substituted halogen is on the aromatic ring and the halide on the benzyl methylene carbon reacts with the amine to form the quaternary compound.
7. The method of claim 6 wherein the halogen substituted benzyl halide is selected from the group consisting of a chlorobenzyl chloride, a fluorobenzyl chloride, bromobenzyl chloride, an iodobenzyl chloride, a chlorotoluene, and a chloromethyl chloronaphthalene.
8. The method of claim 6 wherein the aqueous acid is selected from the group consisting of hydrochloric acid, hydrofluoric acid, acetic acid, formic acid, and mixture of these.
9. The method of claim 8, wherein the quaternary compound comprises from 0.01 to 10.0 vol % of the aqueous acid solution.
10. The method of claim 7 wherein the quaternary compound comprises from 0.05 to 3.0 vol % of the aqueous acid solution.
11. The method of claim 6 wherein the heterocyclic amine is selected from the group consisting of coal tar bases, quinoline, quinaldine, isoquinoline, pyridine, acridene, phenanthradine, and mixtures and substitutions thereof.
12. An inhibited acid comprising
(a) an aqueous solution of a well treating acid selected from the group consisting of hydrochloric acid, hydrofluoric acid, acetic acid, formic acid, and mixtures thereof; and
(b) from about 0.01 to 10.0 vol % of the treating acid of a quaternary compound prepared by reacting a tertiary aromatic heterocyclic amine with a (halo-substituted-aryl) alkyl halide wherein the halogen substitution is on the aromatic ring and the alkyl halide does not enter into the reaction and remains intact on the aromatic ring and the alkyl group contains from 1 to 3 carbon atoms.
13. The inhibited acid of claim 12 wherein the quaternary compound has the formula consisting of ##STR7## wherein ARYL is a heterocyclic ring or rings; N+ is a positively charged nitrogen atom and is part of ARYL; ARYL' is an aromatic ring or rings; R is an alkyl group containing from 1 to 3 carbon atoms and connects N+ to ARYL'; X is a halogen; Y is a halogen substituted on ARYL'; and Z is a halogen or hydrogen substituted on ARYL'.
14. The inhibited acid of claim 12 and further comprising a water soluble surfactant.
15. The inhibited acid of claim 12, further comprising an effective amount of acetylenic alcohol.
16. The inhibited acid of 12, and further comprising formic acid or formamide.
17. The inhibited acid of claim 12, and further comprising potassium iodide or aqueous iodide.
18. The inhibited acid of claim 12 and further comprising a hydrocarbon liquid.
19. The inhibited acid of claim 12 and further comprising acetylenic alcohol, a hydrocarbon liquid, a water wetting surfactant, and formic acid or formamide.
20. A formulation for inhibiting aqueous acid solutions selected from the group consisting of hydrochloric acid, hydrofluoric acid, acetic acid, formic acid and mixtures thereof which comprises
(a) a quaternary compound having the formula ##STR8## wherein ARYL is a heterocyclic ring or rings; N+ is a positively charged nitrogen atom and is part of ARYL; ARYL' is an aromatic ring or rings; R is an alkyl group containing from 1 to 3 carbon atoms and connects N+ to ARYL'; X is a halogen; Y is a halogen substituted on ARYL'; and Z is a halogen or hydrogen substituted on ARYL'; and
(b) an additive selected from the group consisting of acetylenic alcohol, hydrocarbon liquid, water wetting surfactant, formic acid, formamides, and mixtures thereof.
21. A corrosion inhibitor formulation comprising
(a) from 5 to 50 wt % of the corrosion inhibitor having the formula of ##STR9## wherein ARYL is a heterocyclic ring or rings; N+ is a positively charged nitrogen atom and is part of ARYL; ARYL' is an aromatic ring or rings; R is an alkyl group containing from 1 to 3 carbon atoms and connects N+ to ARYL'; X is a halogen; Y is a halogen substituted on ARYL'; and Z is a halogen or hydrogen substituted on ARYL'.
(b) from 5 to 25 wt % of acetylenic alcohol;
(c) from 5 to 20 wt % of a hydrocarbon liquid selected from the group consisting of mineral oil, pine oil, aromatic naptha, and C14 to C20 fatty acids;
(d) from 1 to 10 wt % of a surfactant capable of dispersing the corrosion inhibitor; and
(e) from 10 to 50 wt % of formic acid or formamide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/204,839 USH751H (en) | 1988-06-10 | 1988-06-10 | Method of inhibiting acid corrosion of ferrous metals |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/204,839 USH751H (en) | 1988-06-10 | 1988-06-10 | Method of inhibiting acid corrosion of ferrous metals |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USH751H true USH751H (en) | 1990-03-06 |
Family
ID=22759667
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/204,839 Abandoned USH751H (en) | 1988-06-10 | 1988-06-10 | Method of inhibiting acid corrosion of ferrous metals |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | USH751H (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
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| US5084210A (en) * | 1990-02-07 | 1992-01-28 | Chemlink Incorporated | Corrosion inhibitor |
| US5089153A (en) * | 1990-03-16 | 1992-02-18 | Williams Dennis A | Method of inhibiting corrosion in acidizing wells |
| US5120471A (en) * | 1985-08-14 | 1992-06-09 | Dowell Schlumberger Incorporated | Process and composition for protecting chrome steel |
| US5756004A (en) * | 1997-05-13 | 1998-05-26 | Halliburton Energy Services, Inc. | Quaternary ammonium compounds useful for inhibiting metal corrosion |
| US5939362A (en) * | 1995-03-27 | 1999-08-17 | Nalco/Exxon Energy Chemicals, L.P. | Enhanced corrosion protection by use of friction reducers in conjuction with corrosion inhibitors |
| US20030183808A1 (en) * | 2002-03-28 | 2003-10-02 | Walker Michael L. | Corrosion inhibitor |
| US20040138071A1 (en) * | 2003-01-15 | 2004-07-15 | Gupta D. V. Satyanarayana | Surfactant based viscoelastic fluids |
| US20080146464A1 (en) * | 2006-12-19 | 2008-06-19 | Malwitz Mark A | Corrosion inhibitor composition comprising a built-in intensifier |
| US20110114322A1 (en) * | 2009-11-17 | 2011-05-19 | Ronald Casey Plasier | Surfactant based viscoelastic fluids and methods of using the same |
| US9074289B2 (en) | 2011-11-08 | 2015-07-07 | Nalco Company | Environmentally friendly corrosion inhibitor |
| US10947446B2 (en) * | 2011-11-23 | 2021-03-16 | Saudi Arabian Oil Company | Dual-phase acid-based fracturing composition with corrosion inhibitors and method of use thereof |
| CN115161644A (en) * | 2021-12-17 | 2022-10-11 | 青岛华节鼎孚节能科技有限公司 | Pipeline corrosion inhibitor for vapor-liquid two-phase transportation and preparation method and application thereof |
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| US10947446B2 (en) * | 2011-11-23 | 2021-03-16 | Saudi Arabian Oil Company | Dual-phase acid-based fracturing composition with corrosion inhibitors and method of use thereof |
| CN115161644A (en) * | 2021-12-17 | 2022-10-11 | 青岛华节鼎孚节能科技有限公司 | Pipeline corrosion inhibitor for vapor-liquid two-phase transportation and preparation method and application thereof |
| CN115161644B (en) * | 2021-12-17 | 2023-05-30 | 青岛华节鼎孚节能科技有限公司 | Pipeline corrosion inhibitor for gas-liquid two-phase transportation and preparation method and application thereof |
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