PREPARATION METHOD FOR THE PLANT-BASED NANO CORROSION INHIBITION BACTERICIDE FOR OILFIELD AND APPLICATION THEREOF

Abstract

The present invention discloses a preparation method for the plant-based nano corrosion inhibition bactericide for oilfield, comprising the following steps: Step 1. Prepare the aloin liquid; Step 2. Stir the carbon nanotube, hydroxyethyl methacrylate and acrylic acid to react for 4 h at a constant temperature of 80° C. to get the carbon nanotube after fiber treatment, namely the modified carbon nanotube; Step 3. Mix the aloin liquid with imidazoline-ammonium-salt, add acetonitrile, and then add modified carbon nanotube, increase the temperature to 95° C. stir and react for 12 hours, and filter after naturally cooling down to room temperature and get the carbon nanotube loaded with bactericide; Step 4. Stir the carbon nanotube loaded with bactericide, diphenylmethane diisocyanate and polycaprolactone to react for 6 hours at a constant temperature of 95° C. and in the reaction process, continuously inject helium to get the target bactericide.

Claims

1. A preparation method for the plant-based nano corrosion inhibition bactericide for oilfield, comprising the following steps: Step 1. Prepare the aloin liquid: Step 2. Stir the carbon nanotube, hydroxyethyl methacrylate and acrylic acid to react for 4 h at a constant temperature of 80° C. to get the carbon nanotube after fiber treatment, namely the modified carbon nanotube; Step 3. Mix the aloin liquid with imidazoline-ammonium-salt, add acetonitrile, and then add modified carbon nanotube, increase the temperature to 95° C., stir and react for 12 hours, and filter after naturally cooling down to room temperature and get the carbon nanotube loaded with bactericide; the mass ratio between aloin liquid, imidazoline-ammonium-salt and modified carbon nanotube is 20:15:1: Step 4. Stir the carbon nanotube loaded with bactericide, diphenylmethane diisocyanate and polycaprolactone to react for 6 hours at a constant temperature of 95° C., and in the reaction process, continuously inject helium to get the target bactericide.

2. The preparation method for the plant-based nano corrosion inhibition bactericide for oilfield according to claim 1, wherein the Step 1 specifically comprises: take the fresh aloe leaves for cleaning, disinfection and removing the edges and corners, and then conduct grinding and centrifugal filtration to get aloe juice; sterilize with ultraviolet light, and then perform the decolorization; filter repeatedly to get the aloe polysaccharide solution and concentrate the solution to get the aloin liquid.

3. The preparation method for the plant-based nano corrosion inhibition bactericide for oilfield according to claim 1, wherein in the Step 2, the mass ratio between carbon nanotube, hydroxyethyl methacrylate and acrylic acid is 1:15:12.

4. The preparation method for the plant-based nano corrosion inhibition bactericide for oilfield according to claim 3, wherein in the Step 2, the stirring speed is 160 rpm.

5. An application method of the plant-based nano corrosion inhibition bactericide for oilfield prepared by the preparation method according to claim 1, wherein the sterilization device comprises a sterilizing tank, a filter layer is provided near the bottom of sterilizing tank, on which the bactericide is attached, and an ultrasonic device is equipped in the sterilizing tank; the oilfield sewage is pumped into the sterilizing tank, and the ultrasonic device is turned on, so as to start sterilizing.

6. The application method of the plant-based nano corrosion inhibition bactericide for oilfield according to claim 5, wherein the sterilized oilfield sewage undergoes secondary treatment to realize oilfield reinjection: the secondary treatment includes flocculation, sedimentation, filtration and other operations in order to remove the precipitated minerals in flowback fluid.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0020] FIG. 1 Sterilization performance test results of bactericide prepared in Embodiment 1

[0021] FIG. 2 Application process flow chart of the plant-based nano corrosion inhibition bactericide for oilfield prepared in the present invention

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0022] The preferred embodiment of the present invention is described in combination with the following attached drawings. It should be understood that the preferred embodiment here described is only used for explaining the present invention rather than for restricting the present invention.

EMBODIMENT 1

[0023] For the preparation method for the plant-based nano corrosion inhibition bactericide for oilfield, the steps are as follows:

[0024] (1) Clean the fresh aloe leaves and disinfect with absolute ethyl alcohol. After drying at 30° C. remove the edges and corners and then conduct grinding and centrifugal filtration to get aloe juice. Place the aloe juice in a prepared glass vial and then conduct the sterilization progress with ultraviolet light to get the sterile juice; add activated carbon with a mass concentration of 1.5% into the sterile juice, heat in a water bath of 60° C., adjust the pH to 7.0, perform discoloration for 30 minutes and filter repeatedly to get the aloe polysaccharide solution. Place the aloe polysaccharide solution into a 1 L distilling flask and evaporate about 80% water through decompression concentration at a temperature of 40° C. Add 5(X) mL ethyl acetate to extract for three to five times, and keep the extraction temperature at 50˜55° C. Extract for 40 minutes each time and finally get the aloin liquid.

[0025] (2) Take carbon nanorod with a mass fraction of 1, hydroxyethyl methacrylate with a mass fraction of 15 and acrylic acid with a mass fraction of 12 to react for 4 h at a temperature of 80° C. and stirring at the speed of 160 r/min. and generate a resin containing side chain active hydroxyl as the fiber treatment agent of carbon nanorod to strengthen the absorption performance of carbon nanorod. Filter after naturally cooling down to room temperature for future use.

[0026] (3) Mix the aloin liquid with imidazoline-ammonium-salt of benzoic acid, and add acetonitrile to facilitate their better dissolution where the mass fraction of aloin liquid is 20 and the mass fraction of imidazoline-ammonium-salt is 15. Add the carbon nanorod treated according to Step (2), of which the mass fraction is 1, heat it up to 95° C. and then stir and react for 12 hours. Filter after naturally cooling down to room temperature.

[0027] (4) Mix diphenylmethane diisocyanate with a mass fraction of 10 and polycaprolactone with a mass fraction of 7 with the filtered carbon nanotube that absorbs aloin and imidazoline-ammonium-salt to react for 6 hours at a constant temperature of 95° C. In the whole reaction process, inject helium to fully fix the effective constituents loaded on the carbon nanotube and get the plant-based nano corrosion inhibition bactericide for oilfield prepared in the present invention after naturally cooling down to room temperature.

[0028] Use the bactericide prepared in Embodiment 1 for bactericidal performance test and corrosion inhibition performance test:

[0029] (1) Sterilization Performance Test

[0030] Before the test, all devices and glass containers were sterilized for 20 min at 121° C. The SRB strain was isolated from the formation water of an injection well in a shale gas field in China. SRB liquid medium was prepared according to NACE TMO194-94 standard.

[0031] The composition of the medium is as follows: Ig yeast powder, 0.1 g ascorbic acid, 0.2 g MgSO.sub.4.Math.7H.sub.2O, 0.01 g K.sub.2HPO.sub.4, 10 g NaCl, 0.2 g (NH.sub.4).sub.2Fe(SO.sub.4).sub.2.Math.6H.sub.2O, 4 mL sodium lactate, and 1000 mL deionized water. A portable pressure steam disinfection pot was used to sterilize the bacteria in the prepared medium. In the sterilization process, the temperature was kept at 120° C. for 15 min. It was then deoxidized with N.sub.2 for 2 h. 10% SRB was inoculated into the medium and placed in an incubator at 37° C. After 5 days, the number of SRB reached the peak value and remained stable.

[0032] Different bactericides were added into the cultured bacteria solution of 200 mL and counted 24 hours later.

[0033] Serial dilution method (triple repetition) was taken for the counting of SRB. Totally 10 dilution levels were provided. At each dilution level, there were three identical vials filled with 9 mL SRB medium. The measured sample of 1 mL was injected into a vial at the Level 0 and then shaken up. The 1 mL solution from the vial at the Level 0 was injected into a vial at the Level 1. The syringe for sampling the liquid each time was disposable to avoid affecting the final results. Similarly, the sample was diluted until the dilution reached Level 9. All vials were incubated at 35° C. for 14 days at a constant temperature.

[0034] The growth index should be determined according to the following principles: three dilution levels were selected from the dilution level at which negative vials appeared, and the number of positive vials was counted for each dilution level to obtain the index (When all the vials in a certain grade are negative, the previous grade is counted). The growth index (summarized according to 5.6.5.3 in SY/T 5329-1994) is obtained by multiplying the dilution factor 10.sup.n of water sample (n is the number of dilutions before the index position). Check the corresponding bacteria count table and substitute the bacterial count detected by the index to get the content of this kind of bacteria in the water sample (Nr./mL).

[0035] The test results are shown in Table 1, in which the vials 1 to 10 are filled with 9 mL SRB medium (10.sup.7). The dilution levels are numbered from Lev. 0 to Lev. 9. Take the measured sample of 1 mL into the Vial 1, indicating Level 0; take a new syringe and take 1 mL from Vial 1 to Vial 2, indicating Level 1; take a new syringe and take 1 mL from Vial 2 to Vial 3, indicating Level 3; the rest can be done in the same manner until 1 mL is taken from Vial 9 to Vial 10, indicating Level 9. “+” represents positive vial, and “−” represents negative vial. As shown in FIG. 1, the transparent is the negative vial in which there is no SRB, and the black is the positive vial in which there is SRB.

TABLE-US-00001 TABLE 1 Bactericidal performance test results Vial 1 Vial 2 Vial 3 Vial 4 Vial 5 Vial 6 Vial 7 Vial 8 Vial 9 Vial 10 Growth Number Sterilization Group Level 0 Level 1 Level 2 Level 3 Level 4 Level 5 Level 6 Level 7 Level 8 Level 9 index of SRB rate No bactericide +++ +++ +++ +++ +++ +++ +++ −−− −−− −−− 300 2500000 0 Traditional +++ +++ +++ +++ +++ +++ ++− +−− −−− −−− 210 1500000 40% bactericide 1227 (60 mg/L) Glutaraldehyde +++ +++ +++ +++ +++ +++ ++− −−− −−− −−− 200 900000 64% (60 mg/L) Bactericide in +++ +++ +++ +++ +++ ++− ++− −−− −−− −−− 220 200000 92% Embodiment 1 (60 mg/L)

[0036] (2) Research the interaction between aloin and imidazoline-ammonium-salt: investigate whether there is a synergistic effect between them through the combined index. The combined index formula of the two agents is as follows:

[00001]$\mathrm{CI}=\frac{{\left(D\right)}_1}{{\left(\mathrm{DX}\right)}_1}+\frac{{\left(D\right)}_2}{{\left(\mathrm{DX}\right)}_2}$

[0037] Where, (DX).sub.1 and (DX).sub.2 are respectively the concentration for the sterilization rate of the two agents reaches X % when they are used alone, and (D).sub.1 and (D).sub.2 are the concentrations for the sterilization rate of X % when the two agents are used together. The CI value may represent the combined index of the two agents. If the value is equal to 1, there will be an additive affect. If the value is larger than 1, there will be an antagonistic effect. If the value is smaller than 1, there will be a synergistic effect. If this value is smaller than 0.5, there will be a strong synergistic effect.

[0038] In the embodiment of the present invention, aloin: (D).sub.1=300. (DX).sub.1=1000;

[0039] Imidazoline-ammonium-salt of oleic acid: (D).sub.2=20, (DX).sub.2=90;

[0040] CI.sub.100%=0.52 between aloin and imidazoline-amnmonium-salt of oleic acid, indicating that there is a synergistic sterilization effect between them.

[0041] Imidazoline-ammonium-salt of benzoic acid: (D).sub.2a=35, (DX).sub.2a=95;

[0042] CI.sub.100%=0.67 between aloin and imidazoline-ammonium-salt of benzoic acid, indicating that there is a synergistic sterilization effect between them.

[0043] Imidazoline-ammonium-salt of fatty acid: (D).sub.2b=40, (DX).sub.b=100;

[0044] CI.sub.100%=0.7 between aloin and imidazoline-ammonium-salt of fatty acid, indicating that there is a synergistic sterilization effect between them.

[0045] Therefore, there is a synergistic sterilization effect between aloin and imidazoline-ammonium-salt as specified in the present invention.

[0046] (3) Corrosion inhibition performance test:

[0047] The formula for the corrosive solution is shown in Table 2. The corrosive solution of 1 L was prepared, the pH was adjusted to 6.5, and the temperature was 37° C. at a normal pressure. The N80 steel specimens were processed with specifications of 30*15*3 and placed in corrosive solution. Three specimens were placed in each vial and different corrosion inhibitors were added respectively. The experiment lasted for 14 days.

TABLE-US-00002 TABLE 2 Formula for Corrosive Solution NaCl CaCl.sub.2 MgSO.sub.4 NaHCO.sub.3 NaSO.sub.4 30 g/L 12 g/L 23.6 g/L 10.5 g/L 9.5 g/L

[0048] After the test, the specimens were cleaned with stripping solution (100 ml hydrochloric acid+10 g hexamethylenetetramine+900 mL deionized water), then dehydrated by ethanol and blow-dried with N.sub.2. The determination method for static uniform corrosion inhibition rate was evaluated with referring to the Performance Index and Evaluation Method of Corrosion Inhibitor for Oilfield Produced Water Treatment (SY/T 5273-2014), the oil and gas industry standard of the People's Republic of China. The formulas of uniform corrosion rate and corrosion inhibition efficiency are as follows:

[00002]$r_c=\frac{8.76⨯{10}^4⨯\left(m-m_1\right)}{S⨯t⨯\rho }$

[0049] Where,

[0050] r.sub.c—Uniform corrosion rate, in mm/a;

[0051] m—Mass of the test piece before the test, in g;

[0052] m.sub.1—Mass of the test piece after the test, in g;

[0053] S—Total area of the test piece, in cm.sup.2;

[0054] ρ—Density of the test piece material, in g/cmi;

[0055] t—Test time, in h.

[00003]${\eta }_w=\frac{r_0-r_1}{r_0}⨯100\%$

[0056] Where,

[0057] η.sub.w—Corrosion inhibition efficiency, %;

[0058] r.sub.0—Corrosion rate of blank test piece, in mm/a;

[0059] r.sub.1—Corrosion rate of test piece added with corrosion inhibitor, in mm/a.

[0060] The corrosion inhibition test results are shown in Table 3, in which the corrosion inhibitors 1, 2 and 3 commonly used in oilfields are respectively the lauric acid imidazoline, abietic acid imidazoline and tetradecyl trimethyl ammonium bromide.

TABLE-US-00003 TABLE 3 Corrosion inhibition test results Dosage Corrosion Corrosion inhibition Group (mg/L) rate (mm/a) efficiency Blank — 0.3254 — Lauric acid 60 mg/L 0.0218 93.3% imidazoline Abietic acid 0.0198 93.9% imidazoline Tetradecyl trimethyl 0.0295 90.9% ammonium bromide Bactericide used in 0.0120 96.31% Embodiment 1

[0061] As shown in FIG. 2, the application process of the plant-based nano corrosion inhibition bactericide for oilfield as stated in the present invention is given as follows: The sterilization is performed in a sterilizing tank. A filter layer is provided near the bottom of sterilizing tank, on which the bactericide is fixed, and an ultrasonic device is provided in the sterilizing tank. The flowback fluid is pumped into the sterilizing tank so that SRB in the secondary produced water of oilfield can be attached to the carbon nanotube on the filter layer. The ultrasonic device is turned on so that the bactericide on the carbon nanotube begin to play its bactericidal role, and at the same time the oilfield sewage can be initially treated. The sterilized oilfield sewage undergoes secondary treatment such as flocculation, sedimentation and filtration to remove the precipitated minerals in flowback fluid and realize oilfield reinjection.

[0062] The above are only the preferred embodiments, which are not intended to limit the present invention in any form. Although the present invention has been disclosed as above with preferred embodiments, it is not intended to limit the present invention. Those skilled in the art, within the scope of the technical solution of the present invention, can use the disclosed technical content to make a few changes or modify the equivalent embodiment with equivalent changes. Within the scope of the technical solution of the present invention, any simple modification, equivalent change and modification made to the above embodiments according to the technical essence of the present invention are still regarded as a part of the technical solution of the present invention.