EP0956322A1 - Corrosion inhibitor for wellbore applications - Google Patents

Corrosion inhibitor for wellbore applications

Info

Publication number
EP0956322A1
EP0956322A1 EP96934168A EP96934168A EP0956322A1 EP 0956322 A1 EP0956322 A1 EP 0956322A1 EP 96934168 A EP96934168 A EP 96934168A EP 96934168 A EP96934168 A EP 96934168A EP 0956322 A1 EP0956322 A1 EP 0956322A1
Authority
EP
European Patent Office
Prior art keywords
hydroxide
process according
compound
comprised
composition
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.)
Ceased
Application number
EP96934168A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0956322A4 (enrdf_load_stackoverflow
Inventor
Yulin Wu
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Phillips Petroleum Co
Original Assignee
Phillips Petroleum Co
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 Phillips Petroleum Co filed Critical Phillips Petroleum Co
Priority claimed from PCT/US1996/016352 external-priority patent/WO1998016592A1/en
Publication of EP0956322A1 publication Critical patent/EP0956322A1/en
Publication of EP0956322A4 publication Critical patent/EP0956322A4/xx
Ceased legal-status Critical Current

Links

Definitions

  • This invention relates to a corrosion inhibitor and the use thereof in wellbore
  • Aerated liquids and foams are frequently employed as wellbore fluids during
  • Aerated liquids are distinguishable from foams by
  • Aerated liquids and foams are particularly useful when reduced hydrostatic pressure
  • geological strata at underbalanced conditions i.e., wellbore pressure less than fluid pressure
  • Aerated liquids are nominally comprised of a gas and a liquid and may
  • additives such as corrosion inhibitors and suspended solids such as mud
  • tubing for transporting the gas downhole to an injection point where it is combined with liquid
  • a foam is physically composed of gas bubbles
  • a surfactant-bearing aqueous film surrounded by a surfactant-bearing aqueous film and is nominally comprised of a gas, at least
  • one surfactant which functions as a foaming agent, and water.
  • foam quality is defined to be the volume percent of gas in the two-phase mixture.
  • used in foams may be chemically pure, fresh, or contain varying degrees of salinity and/or
  • the foam may additionally be comprised of other additives which alter the
  • Such additives include selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite which are selected polymers and/or bentonite
  • the rheological properties of foam are complex and provide a separate and
  • foam also possesses at low linear flow velocities excellent carrying capacities
  • downhole operations can be performed without removal of the wellbore tubing.
  • Oxygen generally originates from air.
  • Carbon dioxide and hydrogen sulfide are generally produced from the geological strata of
  • oxygen-bearing gas/liquid mixture suitable for use in wellbore applications including drilling,
  • Still a further object of this invention to develop a corrosion inhibited oxygen-
  • a yet still further object is to develop a process employing foam suitable for use
  • a corrosion-inhibited gas-liquid mixture nominally
  • this invention concerns a unique formulation for a
  • the inventive corrosion inhibitor is nominally comprised of at least one phenolic
  • R b R 2 , R 3 , R 4 and R 5 are independently selected from the group consisting of
  • Flavotannins are polyphenolic materials which are extracted from the bark
  • Quebracho is an example of a suitable flavotannin.
  • Suitable phenolic compounds are those selected from
  • naphthols polyhydroxy naphthols, o-cresol, m-cresol, p-cresol, o-fluorophenol, m-
  • bromophenol bromophenol, m-bromophenol, p-bromophenol, o-iodophenol, m-iodophenol, p-iodophenol,
  • the phenolic compound is more preferably phenol, o-cresol, o-fluorophenol, o-
  • chlorophenol o-bromophenol, o-iodophenol, o-nitrophenol, catechol, resorcinol, guaiacol,
  • hydroquinone hydroquinone, salicylaldehyde, phloroglucinol, pyrogallol, 4,4-biphenol, 1,3-dihydroxy naphthalene or o-allylphenol or any of the salts of the preceding or mixtures thereof of the
  • phenolate salts are those of sodium and
  • phenolic compounds are phenol and the sodium and potassium salts thereof which are sodium
  • the hydroxide-bearing compound must be a compound capable of imparting a
  • hydroxide-bearing compounds are the alkali metal
  • hydroxides ammonium hydroxide or mixtures thereof. More preferred are those selected
  • hydroxide Of these, sodium hydroxide and potassium hydroxide are still more preferred.
  • potassium hydroxide Most preferred is potassium hydroxide.
  • a ratio of about 20 to about 350 is most preferred.
  • hydroxide-bearing compounds consisting of ammonium hydroxide, potassium
  • the corrosion inhibitor may additionally be comprised of water in an amount
  • the water may be chemically pure
  • the inventive corrosion inhibitor is distinguished from many other inhibitors,
  • the corrosion inhibitor is effective at both ambient and elevated
  • inventive inhibitor is also distinguishable from many commercially
  • the corrosion inhibitor is particularly effective when the oxidizing agent is oxygen or
  • the aerated liquid is nominally comprised of a gas which contains
  • the corrosion inhibitor is particularly effective when the
  • oxidizing agents are hydrogen sulfide, carbon dioxide, and oxygen or oxidation-related
  • the water may be chemically pure, fresh, or contain appreciable salinitv and/or hardness and may contain dissolved gases, some of which may favor oxidation.
  • aerated liquid may additionally be comprised of solids such as sand and dirt or a separate
  • Aerated liquids are particularly useful when a reduction in the bulk density of the
  • An aerated liquid is prepared by combining a gas containing at least one
  • the water-based liquid and corrosion inhibitor are first combined to form a
  • the gas is then added via contacting the liquid and gas phases.
  • the latter contacting step is usually
  • the corrosion inhibitor may also be used in well production wherein gas lift
  • the corrosion inhibitor may be combined
  • the reduced hydrostatic head allows the reservoir fluids, which may also be
  • oxidizing agents such as hydrogen sulfide, carbon dioxide, or oxygen and oxidation-related
  • compounds of these agents may be present in either the gas used for the gas lift or in the fluids
  • the required concentration of corrosion inhibitor in the aerated fluid is that amount effective to insure corrosion inhibition over the time frame of interest at the
  • inhibitors are about 0.1 to about 40 wt% and about 0.005 to about 4.0 wt%, respectively. More
  • inhibited aerated liquid may be used in metal-bearing systems at both ambient and elevated
  • oxidizing agent is oxygen or the oxidation-related compounds thereof.
  • the inventive corrosion-inhibited foam is nominally comprised of a dispersed gas
  • the water may be chemically pure, fresh, or contain appreciable salinity and/or hardness, and
  • liquid phase may contain other additives which function to produce a
  • Foam stabilizers are one such example.
  • foam may additionally contain solids such as sand and dirt and/or a separate organic phase.
  • volume percentage of the combined gaseous and liquid phase which is gas is defined
  • the quality of the foam is preferably about 60 to about 99.75% and
  • a stiffer foam may be prepared by adding guar gum or other organic polymers
  • the gaseous phase may initially contain an oxidizing agent or the phase may be
  • oxidizing agents such as oxygen, hydrogen sulfide or carbon dioxide or
  • a gaseous phase comprised in major portion of air is preferred.
  • inhibited foam may be used in metal-bearing systems at both ambient and elevated
  • concentration will be dependent on water salinity and hardness, foaming agent,
  • preferred foaming agents are those possessing a Ross-Miles initial foam height of at least 10
  • height is the sum of foam heights at 0, 1, 2, 5 and 10 min obtained using the Ross-Miles
  • Typical foaming agent concentrations based on active foaming agent concentration. are about 0.005 to about 4.0 wt% based upon the weight of water, corrosion inhibitor and
  • foaming agent in the liquid phase More preferred foaming agent concentrations are about
  • concentrations are about 0.1 to about 0.3 wt% also based on the liquid phase.
  • Preferred foaming agents include one or more of the following:
  • R is cocoyl, lauryl, or oleoyl and M is H or Na;
  • R is cocoyl, palmitoyl, or tall oil
  • R-O-SO 3 M where R is lauryl and M is an ammonium-containing or an alkali metal cation, more
  • M is an ammonium-containing or alkali metal cation, more preferably NH 4 or
  • R is linear C 12 . 14 , linear C 12 . 15 , lauryl, tridecyl, myristyl, or capryl-capryl;
  • M is an ammonium-containing or alkali metal cation, more preferably Na or
  • R is nonyl, octyl, or decyl
  • R is selected from the group consisting of the linear and branch alkyl groups of C 6 , C 8 ,
  • C ⁇ . n C, 0 , C, 0 . I2 , C, 2 , C, 2 . 14 , C 14 , C 12 .i 5 , C 16 , and C 18 isosteryl, lauryl, cetyl, stearyl, oleyl,
  • R is cetyl, lauryl, myristyl, stearyl, coco, hydrogenated tallow, hexadecyl, tallow,
  • CH 2 CH 2 OH and may be the same or different;
  • R is coco, decyl, cetyl, lauryl, or oleyl
  • amido propylbetaines More preferably amido propylbetaines possessing the formula of
  • R is cocyl, lauroyl, isostearoyl, myristoyl, palmitoyl, and most preferably R is cocyl;
  • the preferred foaming agent is comprised of one or more
  • amidopropylbetaines and more preferably comprised of one or more amidopropylbetaines and
  • R is an oleophilic group having from 10 to 18 carbon atoms and M is an alkali metal or ammonium cation.
  • the most preferred foaming agent is comprised of cocoamidopropyl
  • Foam is generally prepared using surface facilities wherein the gas which will
  • this step is conducted by combining the gas and
  • the confining means are those readily available to one skilled in the art and include
  • the foam is generated in the wellbore
  • the foam is generated at the surface by intimately mixing
  • the wellbore fluid is produced via the non-injected tubular or
  • Foam velocity is dependent upon the type of wellbore operation being performed and the designation of said operating conditions is readily within the capabilities of
  • foamer i.e., foaming agent
  • test solutions were prepared from 2% potassium
  • chloride field brine a designated foaming agent, air, and one of two designated and
  • test vessels were constructed of Hastelloy C
  • each vessel contained two 2 1/2 inch x 1/2 inch carbon steel coupons.
  • the coupons
  • test vessels were then pressurized with air to a pressure of 3 psig. The test vessels were then
  • test vessel was then cooled to ambient temperature, the pressure released,
  • test coupons were retrieved and first cleaned using a corrosion-
  • the coupons were further cleaned by contacting with a steel wool pad to
  • the coupons were then weighed and based on the difference between initial and final coupon weights, the corrosion rate was calculated. The
  • Inhibitor A Homco MC-21
  • Inhibitor C Homco AC-105-C
  • Test Series #1 The observed corrosion rate for Run #4 which contained the two corrosion
  • Runs #5 and #6 the corrosion rates were respectively increased by at least 3 -fold and 7-fold.
  • Runs #1 and #2 and for Run #6 presented in Table II for Control Test Series #2.
  • Inhibitor E (Amtech B-1) was used demonstrated relatively low corrosion rates at the test
  • the inhibitors may be obtained from the source identified in Table X.
  • w ⁇ est liquid for each test was 135 ml of 2% KC1 brine and 15 ml kerosene to which was added the identified inhibitors and foamer. Total system volume was approximately 215 ml. c Severe pitting observed.
  • ⁇ est liquid was 135 ml of 2% KC1 brine and 15 ml kerosene to which was added the identified inhibitors and foamer. Total system volume was approximately 215 ml.
  • ⁇ est liquid was 135 ml of 2% KC1 field brine and 15 ml kerosene to which was added the identified inhibitors and foamer. Total system volume was approximately 215 ml. * Homco MC-1
  • Control Test Series #5 provides comparative data regarding the applicability of
  • Inhibitor D (Amtech MC-1), Inhibitor E (Amtech B-1) and Inhibitor F (Baker Cronox C-617)
  • H d was 135 ml of 2% KC1 brine and 15 ml kerosene to which was added the identified and foamer. Total system volume was approximately 215 ml.
  • ⁇ est liquid was 135 ml of 2% KC1 brine and 15 ml kerosene to which was added the identified inhibitors and foamer. Total system volume of approximately 215 ml. iT Severe pitting 'Some pitting
  • the inventive inhibitor was effective at phenol to oxygen molar ratios in
  • Hest liquid was 80 ml of 2% KC1 brine to which was added the above specified chemicals, inhibitors and * foamer. Total system volume was approximately 120 ml.
  • test results confirm at a higher temperature the results presented in Test Series #1.
  • bearing compound capable of imparting a pH of at least 9 to a base aqueous fluid, KOH, or
  • Test Numbers 6-10 similarly concern corrosion inhibition in an air/brine system containing
  • Fluids for Test Numbers 1-5 were prepared from 80 ml of 2% KCI brine to which KOH, phenol and foamer were added in the designated percentages.
  • Fluids for Test Numbers 6-10 were prepared from 65 ml of 2% KCI brine and 15 ml of 60 wt% NH 4 OH to which phenol and foamer were added in the designated percentages. Total system volume was 120 ml.
  • Test conditions were 350°F and 7.6 psig for 42.5 hrs. Overburden gas was air.
  • Foamer was Homco SF-1009

Landscapes

  • Preventing Corrosion Or Incrustation Of Metals (AREA)
EP96934168A 1996-10-15 1996-10-15 Corrosion inhibitor for wellbore applications Ceased EP0956322A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US1996/016352 WO1998016592A1 (en) 1995-06-02 1996-10-15 Corrosion inhibitor for wellbore applications

Publications (2)

Publication Number Publication Date
EP0956322A1 true EP0956322A1 (en) 1999-11-17
EP0956322A4 EP0956322A4 (enrdf_load_stackoverflow) 1999-12-15

Family

ID=22255944

Family Applications (1)

Application Number Title Priority Date Filing Date
EP96934168A Ceased EP0956322A1 (en) 1996-10-15 1996-10-15 Corrosion inhibitor for wellbore applications

Country Status (2)

Country Link
EP (1) EP0956322A1 (enrdf_load_stackoverflow)
CA (1) CA2266624A1 (enrdf_load_stackoverflow)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4089789A (en) * 1972-02-04 1978-05-16 The Richardson Company Corrosion inhibitors
US4376867A (en) * 1981-07-07 1983-03-15 Gert Jansen Chemical process

Also Published As

Publication number Publication date
EP0956322A4 (enrdf_load_stackoverflow) 1999-12-15
CA2266624A1 (en) 1998-04-23

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