ETHYLENEAMINE SULFONATE-BASED SURFACTANT FOR HIGH TEMPERATURE FOAMING
20210163813 · 2021-06-03
Inventors
- Wenke Miao (Shanghai, CN)
- Peng GAO (Shanghai, CN)
- Lixin You (Shanghai, CN)
- Cheng Shen (Shanghai, CN)
- Pramod D. Patil (Sugar Land, TX, US)
- Biplab Mukherjee (Pearland, TX, US)
- Troy E. Knight (Missouri City, TX, US)
Cpc classification
C07C303/28
CHEMISTRY; METALLURGY
C07C233/38
CHEMISTRY; METALLURGY
C07C309/69
CHEMISTRY; METALLURGY
C07C309/14
CHEMISTRY; METALLURGY
C07C231/14
CHEMISTRY; METALLURGY
C09K8/584
CHEMISTRY; METALLURGY
C07C233/36
CHEMISTRY; METALLURGY
International classification
C09K8/584
CHEMISTRY; METALLURGY
C07C231/14
CHEMISTRY; METALLURGY
C07C233/36
CHEMISTRY; METALLURGY
C07C233/38
CHEMISTRY; METALLURGY
C07C303/28
CHEMISTRY; METALLURGY
C07C309/69
CHEMISTRY; METALLURGY
Abstract
Surfactants constructed from three synthetic building blocks that contain multiple hydrocarbon chains, ethyleneamine, and alkyl sulfonate salt groups, were shown to possess good thermal stability, and foamability, and high foam profiles. The materials are targeted for high temperature foaming applications, such as foam flooding enhanced oil recovery to improve conformance control and other oil and gas downhole foaming applications.
Claims
1. A method for treating crude oil, said method comprising: contacting said crude oil with a surfactant in an environment to produce a treated mixture, wherein said surfactant comprises one or more primary components having the chemical formula: ##STR00009## wherein R.sub.1 is a C.sub.5-C.sub.21 linear or branched, saturated or unsaturated alkane; R.sub.2 is a C.sub.3-C.sub.10 linear or branched, saturated or unsaturated alkane; R.sub.3 is selected from the group consisting of Na, K, Ca, and Mg; and n≥1.
2. The method of claim 1, wherein said surfactant further comprises one or more secondary components having the chemical formula: ##STR00010## wherein R.sub.1 is a C.sub.5-C.sub.21 linear or branched, saturated or unsaturated alkane; and m≥1
3. The method of claim 2, wherein m=n+1
4. A method of synthesizing a surfactant, said method comprising the steps of: synthesizing a secondary component by reacting an ethyleneamine with a fatty acid, a solvent, and a weak acid.
5. The method of claim 4, further comprising the steps of: synthesizing a primary component by reacting said secondary component with a sultone compound having a R.sub.2 hydrocarbon chain, an inorganic compound having the formula R.sub.3OH, and an alcohol having the formula R.sub.4OH; wherein R.sub.2 is a C.sub.3-C.sub.10 linear or branched saturated or unsaturated alkane; R.sub.3 is selected from the group consisting of Na, K, Ca, and Mg; R.sub.4 is a C.sub.2-C.sub.3 linear or branched, saturated or unsaturated alkane; and n≥1.
6. The method of claim 5, wherein said ethyleneamine is selected from the group consisting of diethylenetriamine (DETA), triethylene tetramine (TETA), tetraethylene pentamine (TEPA), pentaethylene hexamine (PEHA), hexaethylene heptamine (HEHA) and mixtures thereof.
7. The method of claim 5, wherein said fatty acid is capric acid.
8. The method of claim 5, wherein said solvent is xylene.
9. The method of claim 5, wherein said weak acid is orthoboric acid.
10. The method of claim 5, wherein: said ethyleneamine has a molecular weight between approximately 100 g/mol. and approximately 325 g/mol.; and said fatty acid has a molecular weight between approximately 100 g/mol. and approximately 300 g/mol.
11. The method of claim 5, wherein: said weak acid is between approximately 0.01 wt. % to approximately 2.0 wt. % of the total solution; said sultone compound having a R2 hydrocarbon chain is between approximately 5.0 wt. % to approximately 35.0 wt. % of the total solution; said inorganic compound having the formula R.sub.3OH is between approximately 2.0 wt. % to approximately 12.0 wt. % of the total solution; and said alcohol having the formula R.sub.4OH is between approximately 30.0 wt. % to approximately 70.0 wt. % of the total solution.
12. The method of claim 4, further comprising the steps of: synthesizing said primary component by reacting said secondary component at 50° C. with C.sub.5H.sub.5N, H.sub.2O and a composition having the chemical formula: ##STR00011##
13. The method of claim 4, further comprising the steps of: synthesizing said primary component by reacting said secondary component with p-Tosyl Chloride, NaOH, Na.sub.2SO.sub.3, NaNO.sub.3, H.sub.2O and a composition having the chemical formula: ##STR00012##
14. The method of claim 4, further comprising the steps of: synthesizing said primary component by reacting said secondary component with H.sub.2O and a composition having the chemical formula: ##STR00013##
15. The method of claim 4, further comprising the steps of: synthesizing said primary component by reacting said secondary component at 100° C. with NaOH, H.sub.2O and a composition having the chemical formula: ##STR00014##
16. A surfactant for treating crude oil, said surfactant comprising one or more first one or more primary components having the chemical formula: ##STR00015## wherein R.sub.1 is a C.sub.5-C.sub.21 linear or branched, saturated or unsaturated alkane; R.sub.2 is a C.sub.3-C.sub.10 linear or branched saturated or unsaturated alkane; and n≥1.
17. The surfactant of claim 11, wherein said surfactant further comprises one or more secondary components having the chemical formula: ##STR00016## wherein R.sub.1 is a C.sub.5-C.sub.21 linear or branched, saturated or unsaturated alkane; and m≥1.
18. The method of claim 1, wherein said primary component has a concentration between approximately 5.0 ppm to 50,000 ppm.
19. The method of claim 2, wherein said secondary component has a concentration between approximately 5.0 ppm to 50,000 ppm.
20. The method of claim 1, wherein the temperature of said environment is between 100° C.-300° C.
Description
BRIEF DESCRIPTION OF THE FIGURES
[0009]
[0010]
[0011]
[0012]
[0013]
[0014]
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0015] A representative synthesis reaction for the surfactant of the invention is as follows:
##STR00001##
wherein R.sub.1 is a C.sub.5-C.sub.21 linear or branched, saturated or unsaturated alkane; R.sub.2 is a C.sub.3-C.sub.10 linear or branched, saturated or unsaturated alkane; R.sub.3 is Na, K, Ca, or Mg; R.sub.4 is a C.sub.2-C.sub.3 linear or branched, saturated or unsaturated alkane; and n ≥1. Preferred solvents include, but are not limited to xylene. As the above reaction shows, the novel surfactant is synthesized by reacting an ethylene amine with an acid in solvent to form a solution, and then further treating the solution with a weak acid to form an intermediate amide. The intermediate amide is then reacted with a sultone, an inorganic alkali, and an alcohol as solvent, resulting in the novel surfactant.
[0016] Alternate methods of synthesizing the novel surfactant via an intermediate amine are as follows:
##STR00002##
Ethyleneamine
[0017] The surfactant of the invention utilizes as a precursor an ethyleneamine having the generic formula:
##STR00003##
wherein n ≥1. Ethyleneamines are the preferred backbone for the surfactant of the invention as these molecules have more than two active sites (NH.sub.2 and/or NH) that allow for amide functional groups in the system. The amide groups readily form intermolecular or intramolecular hydrogen bonds to stabilize surfactants along the foam bubble surface. Preferred ethyleneamines for the novel surfactant include Diethylenetriamine (DETA), Triethylene tetramine (TETA), Tetraethylene pentamine (TEPA), Pentaethylene hexamine (PEHA), Hexaethylene heptamine, (HEHA) and mixtures thereof. Preferably, ethyleneamines with a molecular weight between approximately 100 g/mol. and approximately 325 g/mol. are utilized in the surfactant synthesis reaction.
Fatty Acid
[0018] In addition to ethyleneamines, the surfactant of the invention also utilizes as a precursor fatty acids having the following chemical formula:
##STR00004##
[0019] wherein R.sub.1 is a C.sub.5-C.sub.21 linear or branched, saturated or unsaturated alkane. As the above formula shows, fatty acids are carboxylic acids with long unbranched aliphatic chains, which, when synthesized with ethyleneamines, result in hydrophobic tails for the surfactant of the invention. Preferred fatty acids for the synthesis of the surfactant of the invention include, but are not limited to, capric acid. Preferably, fatty acids with a molecular weight between approximately 100 g/mol. and approximately 300 g/mol. are utilized in the surfactant synthesis reaction.
Weak Acid
[0020] A weak acid is utilized as a catalyst to facilitate amidation reaction of the fatty acid and ethyleneamine to form the surfactant precursor. Preferred weak acids include, but are not limited to, orthoboric acid. Preferably, approximately 0.01 wt. % to approximately 2.0 wt. % of weak acid is utilized in the surfactant synthesis reaction.
Sulfonate Salt
[0021] The surfactant of the invention incorporates a sulfonate salt. The sulfonate salt is incorporated in the novel surfactant by reacting the intermediate amide with a sultone having a R.sub.2 carbon chain, an inorganic compound having the formula R.sub.3OH, and an alcohol having the formula R.sub.4OH, wherein R.sub.2 is a C.sub.3-C.sub.10 linear or branched, saturated or unsaturated alkane; R.sub.3 is Na, Ca, or Mg; and R.sub.4 is a C.sub.2-C.sub.3 linear or branched, saturated or unsaturated alkane. The alcohol may be a primary or secondary alcohol. Preferably, approximately 5.0 wt. % to approximately 35.0 wt. % of R.sub.2-sultone; approximately 2.0 wt. % to approximately 12.0 wt. % of R.sub.3OH, and approximately 30.0 wt. % to approximately 70.0 wt. % of R.sub.4OH are utilized in the surfactant synthesis reaction.
Alternate Methods
[0022] The surfactant of the invention may also be synthesized by reacting the intermediate amide with a compound having the chemical formula:
##STR00005##
along with a C.sub.5H.sub.5N reagent, and utilizing H.sub.2O as a solvent, at 50° C. Preferably, approximately 10.0 wt. % to approximately 70.0 wt. % of the compound; approximately 0.1 wt. % to approximately 10.0 wt. % of the C.sub.5H.sub.5N reagent and approximately 10.0 wt. % to approximately 90.0 wt. % of the H.sub.2O solvent are utilized in this alternate synthesis reaction.
[0023] The surfactant of the invention may also be synthesized by reacting the intermediate amide with a compound having the chemical formula:
##STR00006##
along with p-Tosyl Chloride, a reagent comprising a mixture of NaOH, Na.sub.2SO.sub.3, and NaNO.sub.3, and utilizing H.sub.2O as a solvent. Preferably, approximately 5.0 wt. % to approximately 50.0 wt. % of the compound; approximately 1.0 wt. % to approximately 30.0 wt. % of p-Tosyl Chloride, approximately 1.0 wt. % to approximately 20.0 wt. % of the NaOH reagent, approximately 0.1 wt. % to approximately 15.0 wt. % of the Na.sub.2SO.sub.3 reagent, approximately 0.1 wt. % to approximately 15.0 wt. % range of the NaNO.sub.3, reagent, and approximately 10.0 wt. % to approximately 90.0 wt. % of the H.sub.2O solvent are utilized in this alternate synthesis reaction.
[0024] The surfactant of the invention may also be synthesized by reacting the intermediate amide with a compound having the chemical formula:
##STR00007##
utilizing H.sub.2O as a solvent. Preferably, approximately 15 wt. % to approximately 85 wt. % of the compound and approximately 10.0 wt. % to approximately 90.0 wt. % of the H.sub.2O solvent are utilized in this alternate synthesis reaction.
[0025] The surfactant of the invention may also be synthesized by reacting the intermediate amide with a compound having the chemical formula:
##STR00008##
along with a NaOH reagent and utilizing H.sub.2O as a solvent, at 100° C. Preferably, approximately 20.0 wt. % to approximately 85.0 wt. % range of the compound; approximately 5.0 wt. % to approximately 50.0 wt. % of the NaOH reagent and approximately 10.0 wt. % to approximately 90.0 wt. % of the H.sub.2O solvent are utilized in this alternate synthesis reaction.
Method of Use
[0026] Both the novel surfactant and intermediate amide may be utilized for oilfield applications, especially enhanced oil recovery processes such as foam flooding. A dilute solution of the novel surfactant, or a mixture of the novel surfactant and intermediate amide, is injected into a crude oil reservoir to lower the interfacial tension or capillary pressure that impedes the crude oil from moving through the reservoir. The novel surfactant can be utilized in concentrations of 5.0 ppm to 50,000 ppm, while the intermediate amide can be used in concentrations of 0.0 ppm to 50,000 ppm. The enhanced foaming properties of the novel surfactant and intermediate amide allow the substances to be used in environments where the temperature is up to 300° C. and the salinity is up to 20.0 wt. %. The novel surfactant and intermediate amide can be used alone as the primary foamer or as a co-surfactant with other foaming surfactants such as anionic surfactants—alpha olefin sulfonates (AOS) and internal olefin sulfonates (IOS), nonionic alkoxylate surfactants, cationic surfactants, or blends of anionic and nonioinic foaming agents.
Working Examples
[0027] The following Examples illustrate various representative attributes of the invention but should in no way be construed as limiting.
[0028] Synthesis of DETA-C10-Amine Intermediate
[0029] DETA (1.0 eq) was dissolved in xylene, then capric acid (1.05 eq) (also dissolved in xylene) was added into the DETA-xylene solution drop by drop at a temperature of 60° C. When completed, orthoboric acid (0.005 eq) was added into the mixture and stirred at a temperature of 100° C. for 0.5 hours, then heated to reflux at 150° C. for 14 hours to remove water generated from reaction. The solvent was removed via vacuum evaporation and the remaining composition was recrystallized three times by petroleum ether/ethyl acetate to produce the intermediate
[0030] DETA-C10-Amine. Yield of the intermediate DETA-C10-Amine was greater than 90.0%.
[0031] Synthesis of DETA-C10-SS
[0032] An 8.0 wt. % alkali solution was first prepared by dissolving sodium hydroxide (0.5 eq) into H.sub.2O-EtOH (2.5 wt. %:97.5 wt. %). DETA-C10-Amine (1.0 eq), 1,3-propane sultone (0.5 eq) and ethanol were charged into a three-neck round bottle flask and heated at 60° C. for 6 hours. The resulting mixture was cooled down to room temperature, then one-half of the alkali solution was added dropwise into the mixture and stirred for 0.5 hours. An additional 0.25 eq of 1,3-propane sultone was then added at room temperature, and the mixture was heated to 60° C. for another 4 hours. The mixture was then cooled down to room temperature and another 0.25 eq of alkali solution was added. This process was repeated twice by adding 0.125 eq of 1,3-propane sultone and alkali solution separately, and heated at 60° C. until the reaction completed. The mixture was then concentrated and recrystallized 3 times with ethanol/petroleum ether to produce the target product DETA-C10-SS. Yield of DETA-C10-SS was greater than 60.0%.
[0033] Synthesis of TETA-C10-Amine Intermediate
[0034] TETA (1.0 eq) was dissolved in xylene, then capric acid (2.1 eq) (also dissolved in xylene) was added into the TETA-xylene solution drop by drop at a temperature of 60° C. When completed, orthoboric acid (0.01 eq) was added into the mixture and stirred at a temperature of 100° C. for 0.5 hours, then heated to reflux at 150° C. for 14 hours to remove water generated from reaction. The solvent xylene was removed via vacuum evaporation and the remaining composition was recrystallized 3 times by petroleum ether/ethyl acetate to produce the intermediate TETA-C10-Amine. Yield of the intermediate TETA-C10-Amine was greater than 90.0%.
[0035] Synthesis of TETA-C10-SS
[0036] An 8.0 wt. % alkali solution was first prepared by dissolving sodium hydroxide (1.0 eq) into H.sub.2O-EtOH (2.5 wt. %:97.5 wt. %). TETA-C10-Amine (1.0 eq), 1,3-propane sultone (1.0 eq) and isopropanol were charged into a three-neck round bottle flask and heated at 60° C. for 6 hours. The resulting mixture was cooled down to room temperature, then one-half of the alkali solution was added dropwise into the mixture and stirred for 0.5 hours. An additional 0.5 eq of 1,3-propane sultone was then added at room temperature, and the mixture was heated to 60° C. for another 4 hours. The mixture was then cooled down to room temperature and another 0.5 eq of alkali solution was added. This process was repeated twice by adding 0.25 eq of 1,3-propane sultone and alkali solution separately, and heated at 60° C. until the reaction completed. The mixture was then concentrated and recrystallized 3 times with isopropanol/petroleum ether to produce the target product TETA-C10-SS. Yield of TETA-C10-SS was greater than 70.0%.
Thermal Stability
[0037] The thermal stability of DETA-C10-SS and TETA-C10-SS were evaluated by thermogravimetric analysis (“TGA”) under air and N.sub.2 atmospheres. As shown in
Foaming Performance
[0038] Ross-Miles Testing
[0039] The foamability of the novel surfactants was first measured according to the Ross-Miles method. 200 mL of 0.1 wt. % DETA-C10-SS/DI water solution was poured into a long glass tube, and the foam height was visually checked and recorded every minute. Similarly, 200 mL of 0.1 wt. % TETA-C10-SS/DI water solution was poured into a long glass tube, and the foam height was visually checked and recorded every minute. The results of the testing are depicted in
[0040] As shown in
[0041] It is believed that the chemical structure of each of the novel surfactants is responsible for the surfactants' different foamabilities (measured by foam height) and foam stabilities. Specifically, DETA-C10-SS contains two long hydrophobic linear carbon chains, which maximizes foam height. Moreover, DETA-C10-SS contains two amido groups, which can form intermolecular hydrogen bonds to maintain foam stability. In contrast, TETA-C10-SS contains one hydrophilic (CH.sub.2).sub.3SO.sub.3Na chain, which leads to increased branching and decreases foam stability.
[0042] Foam Scanning
[0043] The foaming properties of the novel surfactant solutions were evaluated using a Teclis ITConcept Foamscan device. A 60.0 mL sample of 0.1 wt. % DETA-C10-SS/DI water solution was injected into a reservoir and a constant air flow of 100 mL/min was bubbled into the solution to generate foam. The sample was foamed for 60 seconds after which the foam volume and conductance were measured respectively by the Foamscan program. The procedure was then repeated with a 60 mL sample of 0.1 wt. % TETA-C10-SS/DI water solution. The results of the Foamscan analysis are depicted in
[0044] As the data in
[0045] Finally, foam scanning of 0.03 wt. % surfactant solutions of DETA-C10-SS and TETA-C10-SS were evaluated at both an elevated temperature of 80° C., as well as an elevated temperature of 80° C. and a salinity of 12.0 wt. % TDS. Additionally, samples were tested at room temperature, as well as at room temperature and a salinity of 12.0 wt. % TDS. The results, which are depicted in
[0046] Although the invention has been described by reference to its preferred embodiment as is disclosed in the specification and drawings above, many more embodiments of the invention are possible without departing from the invention. Thus, the scope of the invention should be limited only by the appended claims.