Formulations of copolymers based on alkyl acrylates used as defoamers of heavy and super-heavy crude oils

Abstract

This invention is directed to a method for defoaming crude oil by the addition of copolymers based on silicone free alkyl acrylics defoamers for crude oils with densities between 10 and 40 API. The alkyl acrylic copolymers at conditions similar to those of gas-liquid separators are efficient foam formation inhibitors in heavy and super-heavy crude oils to reduce foam levels between 15 and 50% faster than non-dosed crude oil. Some acrylic copolymers exhibited a greater efficiency as defoamers than commercial silicones, which promote the defoaming only 20 or 25 vol % faster than the natural foam collapse. Silicones as defoamers present serious problems as the formation of deposits and the deactivation of catalysts in the refining processes. These problems have originated a series of interdictions to use silicon based defoamers and new chemical compounds completely silicon free are required to control the foam levels in the gas/petroleum separation tanks.

Claims

1. A process for defoaming gasified crude oil, said process comprising the step of the addition of a defoaming composition to the gasified crude oil in a degasifying apparatus and defoaming the gasified crude oil, wherein the gasified crude oil has a density of 10 to 40 API and the defoaming composition consisting of at least one copolymer of formula (1) having an average molecular weight between 1000 and 180,000 Dalton dissolved in an organic solvent and contains no water, to reduce foam formation at least 20 vol % compared with a non-dosed gasified crude oil ##STR00003## where: R.sup.1, R.sup.2, R.sup.3 and R.sup.4 are independent radicals represented by the groups mentioned bellow: R.sup.1 and R.sup.3H (hydrogen), CH.sub.3 (methyl); R.sup.2 and R.sup.4 are different and independently selected from the group consisting of CH.sub.3 (methyl), C.sub.2H.sub.5 (ethyl), C.sub.4H.sub.9 (n-butyl, isobutyl), C.sub.6H.sub.13 (n-hexyl, iso-hexyl), C.sub.8H.sub.17 (2 ethyl-hexyl), C.sub.8H.sub.17 (n-octyl), C.sub.10H.sub.21 (n-decyl, iso-decyl), C.sub.12H.sub.25 (n-dodecyl), C.sub.18H.sub.37 (n-octadecyl), C.sub.8H.sub.9O (2-phenoxyethyl), C.sub.3H.sub.7O (2-methoxyethyl), or C.sub.5H.sub.11O.sub.2 (2-(2-methoxyethoxy)ethyl), where the aliphatic chain may contain heteroatoms of the ether group, aromatic rings or rings with heteroatoms of ether type, x=is a number between 2 and 900 y=is a number between 2 and 900 and x and y vary randomly along the copolymer chain.

2. The process according to claim 1, where the copolymers are obtained from monomers consisting of monomers selected from the group consisting of methyl acrylate, ethyl acrylate, butyl acrylate, n-amyl acrylate, isobornyl acrylate, isobutyl acrylate, tert-butyl acrylate, hexyl acrylate, 2-ethylhexylacrylate, 3.5,5-trimethylhexyl acrylate, 2-methoxyethyl acrylate, 2-phenoxy acrylate, 4-tert-butylacyclehexyl acrylate, octyl acrylate, isodecyl acrylate, decyl acrylate, lauryl acrylate, tridecyl acrylate, octadecyl acrylate and behenyl acrylate.

3. The process according to claim 1, where the average molecular mass of copolymers vary between 7,000 and 120,000 Daltons.

4. The process according to claim 1 where an aqueous phase present during the synthesis of said copolymers is eliminated by distillation at a temperature between 80 and 120 C.

5. The process according to claim 1, where the organic solvents have a boiling point between 35 and 200 C.

6. The process according to claim 1, where the organic solvent is dichloromethane, methanol, ethanol, isopropanol, chloroform, benzene and their sub-products, toluene, xylene, turbosine and naphtha, individually or mixtures thereof.

7. The process according to claim 1, where the alkyl acrylate copolymer formulated with said solvent has a concentration between 10 and 50 wt % based on the total weight of the formulation.

8. The process according to claim 1, where the crude oil has a density of less than 20 API.

9. The process according to claim 1 where two or more copolymers based on alkyl acrylates are mixed in said formulation.

10. The process according to claim 1, where said formulations are dosed at a concentration between 10 and 2000 ppm based on the amount of crude oil.

11. The process according to claim 1, wherein x=is a number between 20 and 850, and y=is a number between 20 and 850.

12. The process according to claim 1, wherein x=is a number between 60 to 600, and y=is a number 60 to 600.

13. The process according to claim 7, wherein said formulation comprises 20 to 40 wt % of said compound of formula (1).

14. The process according to claim 10, wherein said process further comprises adding said formulation to said crude oil in an amount of 100 to 1500 ppm based on the amount of the crude oil.

15. The process according to claim 10, wherein said process further comprises adding said formulation to said crude oil in an amount of 200 to 1000 ppm based on the amount of the crude oil.

16. The process according to claim 1, wherein said crude oil has a density of 12 to 22 API.

17. The process of claim 1, wherein an aqueous phase present during synthesis of said copolymers is removed by distillation at a temperature between 90 and 110 C.

18. A process for inhibiting or reducing foam formation of heavy gasified crude oil in a degasifying apparatus, said process comprising the step of introducing an antifoaming agent composition into the separation apparatus containing gasified crude oil having a density of 10 to 40 API and defoaming or reducing foam formation by at least in 20% by volume relative to the gasified crude oil without the antifoaming agent, wherein said antifoaming agent composition comprises an alkyl acrylate copolymer of formula (1) having a molecular weight of 1,000 to 180,000 Daltons and an organic solvent ##STR00004## where: R.sup.1 and R.sup.2 are independently selected from the group consisting of H (hydrogen) and CH.sub.3 (methyl); R.sup.2 and R.sup.4 are different and independently selected from the group consisting of behenyl, 2-phenoxyethyl, 2-methoxyethyl, 2-(2-methoxyethoxy)-ethyl, isobornyl, and butyl cyclohexyl; and x and y are an integer number from 2 to 900, and where said acrylate copolymer is introduced in an amount of 100 to 1500 ppm based on the amount crude oil.

19. The process of claim 18, wherein said antifoaming agent composition consists of said alkyl acrylate copolymer and a solvent.

20. The process of claim 1, wherein said copolymer is selected from the group consisting of R.sup.2 is n-butyl, R.sup.3 is hydrogen, and R.sup.4 is n-hexyl; R.sup.2 is n-butyl, R.sup.3 is hydrogen, and R.sup.4 is n-lauryl; R.sup.2 is n-hexyl, R.sup.3 is hydrogen, and R.sup.4 is phenoxyethyl; R.sup.1 is hydrogen, R.sup.2 is n-hexyl, R.sup.3 is hydrogen, and R.sup.4 is n-octyl; R.sup.1 is hydrogen, R.sup.2 is n-hexyl, R.sup.3 is hydrogen, and R.sup.4 is n-lauryl; and R.sup.1 is hydrogen, R.sup.2 is n-lauryl, R.sup.3 is hydrogen, and R.sup.4 is n-octyl.

21. The process according to claim 18, wherein said copolymer of formula (1) is obtained from monomers consisting of monomers selected from the group consisting of behenyl acrylate, butyl acrylate, 2-phenoxyethyl acrylate, 2-methoxyethyl acrylate, 2-(2-methoxyethoxy)-ethyl acrylate, isobornyl, and butyl cyclohexyl acrylate.

Description

BRIEF DESCRIPTION OF THE DRAWINGS OF THE INVENTION

(1) FIGS. 1 to 6 show the results of the evaluations conducted to determine the performance of these polymers based on alkyl acrylates as new antifoaming agents for gasified heavy crude oils with 15.00 API. Similarly, FIGS. 7 to 12 present the results of the copolymers based on alkyl acrylates evaluated in gasified super-heavy crude oil with 12.84 API.

(2) FIG. 1 shows the performance in the chemical composition of the Co(AB-AH)-1 copolymer (AB/AH: 70/30 wt %) and the Co(AB-AH)-2 copolymer (AB/AH: 30/70 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API; both copolymers were dosed at 500 ppm and compared with the commercial silicon-based product IMP-Si-1.

(3) FIG. 2 shows the performance in the chemical composition of the Co(AB-AL)-1 copolymer (AB/AL: 70/30 wt %) and the Co(AB-AL)-2 copolymer (AB/AL: 30/70 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm and compared with a commercial silicon-based product IMP-Si-1.

(4) FIG. 3 shows the performance in the chemical composition of the Co(AH-AEM)-1 copolymer (AH/AEM: 70/30 wt %) and the Co(AH-AEM)-2 copolymer (AH/AEM: 30/70 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm and compared with a commercial silicon based product IMP-Si-1.

(5) FIG. 4 shows the performance in the chemical composition of the Co(AH-AOc)-1 copolymer (AH/AOc: 30/70 wt %) and the Co(AH-AOc)-2 copolymer (AH/AOc: 70/30 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm and compared with the commercial silicone-based product IMP-Si-1.

(6) FIG. 5 shows the performance in the chemical composition of the Co(AH-AL)-1 copolymer (AH/AL: 30/70 wt %) and the Co(AH-AL)-2 copolymer (AH/AL: 70/30 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm and compared with the commercial silicon-based IMP-Si-1 product.

(7) FIG. 6 shows the performance in the chemical composition of the Co(AL-AOc)-1 copolymer (AL/AOc: 30/70 wt %) and the Co(AL-AOc)-2 copolymer (AL/AOc: 70/30 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm and compared with the commercial silicon-based product IMP-Si-1.

(8) FIG. 7 shows the performance in the chemical composition of the Co(AB-AH)-1 copolymer (AB/AH: 70/30 wt %) and the Co(AB-AH)-2 copolymer (AB/AH: 30/70 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm dose and compared with the commercial silicon-based product IMP-Si-1.

(9) FIG. 8 shows the performance in the chemical composition of the Co(AB-AL)-1 copolymer (AB/AL: 70/30 wt %) and the Co(AB-AL)-2 copolymer (AB/AL: 30/70 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm and compared with the commercial silicon-based product IMP-Si-1.

(10) FIG. 9 shows the performance in the chemical composition of the Co(AH-AEF)-1 copolymer (AH/AEF: 70/30 wt %) and the Co(AH-AEF)-2 copolymer (AH/AEF: 30/70 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm and compared with the commercial silicon-based product IMP-Si-1.

(11) FIG. 10 shows the performance of the chemical composition of the Co(AH-AOc)-1 copolymer (AH/AOc: 70/30 wt %) and the Co(AH-AOc)-2 copolymer (AH/AOc: 30/70 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm and compared with the commercial silicon-based product IMP-Si-1.

(12) FIG. 11 shows the performance in the chemical composition of the Co(AH-AL)-1 copolymer (AH/AL: 70/30 wt %) and the Co(AH-AL)-2 copolymer (AH/AL: 30/70 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm and compared with the commercial silicon-based product IMP-Si-1.

(13) FIG. 12 shows the performance in the chemical composition of the Co(AL-AOc)-1 copolymer (AL/AOc: 70/30 wt %) and the Co(AL-AOc)-2 copolymer (AL/AOc: 30/70 wt %), which were evaluated as antifoaming agents in gasified heavy crude oil with 15.00 API, both copolymers were dosed at 500 ppm and compared with the commercial silicon-based product IMP-Si-1.

DETAILED DESCRIPTION OF THE INVENTION

(14) The present invention relates to the synthesis of copolymers based on alkylacrylates (polymers based on random sequences of two monomers in the polymer chain) and the use as antifoaming agents of gasified heavy and super-heavy crude oils. The random copolymers based on alkyl acrylates show excellent performance as a foam inhibitor and foam suppressor in gasified crude oil. These new antifoaming agents were compared with a commercial silicon-based product IMP-Si-1 at the same concentrations. The results in Mexican patent MX/a/2013/014352 has been aided to carry out this document.

(15) To prepare the formulation of copolymers based on alky acrylate copolymer as defoamers the following method was used. This method is illustrative and does not imply any limitation:

(16) Copolymers based on alkyl acrylate were synthesized by semi-continuous emulsion polymerization as latex, synthesis method described in the U.S. Patent 20110067295A1 (Castro, 2011). A latex is a particle polymeric dispersion in water, easily to process by avoiding to use organic solvents. The water is distilled at temperatures between 80 to 120 C., and an organic solvent is added to obtain the formulation in order to carry out the application of the product as defoamers of gasified crude oils with densities between 10 to 40 API, using solvents having a boiling point falling within the temperature range between 35 to 200 C. The solvent can be dichloromethane, methanol, ethanol, isopropanol, chloroform, benzene and their sub-products, toluene, xylene, turbosine and naphtha, individually or mixed. The amount of copolymer in the resulting solution and formulation is between 10 and 50 wt % and more preferably between 20 and 40 wt %. The formulation can be based on two or more alkyl acrylate copolymers, or a mixture of alkyl acrylate homopolymers and copolymers.

(17) In scheme (1) the copolymer general structure (a random combination of a couple of monomers) of the different alkyl acrylate copolymers of this invention is shown, wherein:

(18) ##STR00002##
where: R.sup.1, R.sup.2, R.sup.3 and R.sup.4 are independent radicals represented by the groups mentioned bellow: R.sup.1 and R.sup.3H (hydrogen), CH.sub.3 (methyl); R.sup.2 and R.sup.4CH.sub.3 (methyl), C.sub.2H.sub.5 (ethyl), C.sub.4H.sub.9 (n-butyl, isobutyl), C.sub.6H.sub.13 (n-hexyl, iso-hexyl), C.sub.8H.sub.17 (2 ethyl-hexyl), C.sub.8H.sub.17 (n-octyl), C.sub.10H.sub.21 (n-decyl, iso-decyl), C.sub.12H.sub.25 (n-dodecyl), C.sub.18H.sub.37 (n-octadecyl), C.sub.8H.sub.9O (2-phenoxyethyl), C.sub.3H.sub.7O (2-methoxyethyl), C.sub.5H.sub.11O.sub.2 (2-(2-methoxyethoxy)ethyl). This aliphatic chain may contain heteroatoms of the ether group, aromatic rings or rings with heteroatoms of ether type. where x and y are numbers within the following ranges: x=is a number from 2 to 900. y=is a number from 2 to 900. x and y vary randomly along the copolymer chain. In one embodiment, x can be 20 to 850 and y can be 20 to 850. In a further embodiment, x can be 60 to 600 and y can be 60 to 600.

(19) Additionally, the molecular weights of the copolymers range from 1000 to 180 000 Daltons, preferably from 7000 to 120 000 Daltons.

(20) The following describes by way of example, it does not imply any limitation, the monomers used in the synthesis of the copolymers object of this invention: methyl acrylate, ethyl acrylate, butyl acrylate, n-amyl acrylate, isobornyl acrylate isobutyl acrylate, tert-butyl acrylate, hexyl acrylate, 2-ethylhexyl acrylate, 3,5,5-trimethylhexyl acrylate, 2-methoxiethyl acrylate, 2-phenoxiethyl acrylate, 4-tert-butylcyclohexyl acrylate, octyl acrylate, isodecyl acrylate, decyl acrylate, lauryl acrylate, tridecyl acrylate, octadecyl acrylate or behenyl acrylate.

(21) The method of inhibiting foam formation or defoaming crude oil includes the step of adding an effective amount of the copolymer based on alkyl acrylate to gasified crude oils with densities from 10 to 40 API, and at concentrations between 10 and 2000 ppm based on the amount of crude oil, in order to inhibit the formation of foam. The copolymer can have a molecular weight of 1000 to 180,000 Dalton. The crude oil in one embodiment contains a dissolved gas where the copolymer is added in an amount to prevent or inhibit foaming during degasification or processing of the crude oil that can cause the dissolved gas to separate from the crude oil. The defoaming agent of the invention containing the copolymer can be present is the crude oil when the crude oil is supplied or fed to the degasifying apparatus. The formulation can be combined with the crude oil in an amount of 10 to 2000 ppm based on the amount of the crude oil. In other embodiments, the formulation is combined in an amount of about 100 to 500 ppm based on the amount of crude oil. In further embodiments, the formulation is combined with the crude oil in an amount of about 200 to 1000 ppm based on the amount of crude oil.

(22) The present invention is described in respect to specific number of examples, which are considered as illustrative and does not mean limitation. Once obtained, the copolymers based on alkyl acrylate were characterized using the following instrumental methods:

(23) 1.Size exclusion chromatograph Agilent model 1100, with PLgel column and using tetrahydrofuran (THF) as eluent, to calculate the copolymers molecular mass distribution and polydispersity index (I).

(24) 2.Fourier Transform Infrared band spectrometer model Thermo Nicolet AVATAR 330 using the method of film technique with software OMNIC version 7.0.

(25) Average molecular masses, polydispersity index and spectroscopic characteristics of the copolymers based on alkyl acrylate are described in Tables 1-6, which does not imply any limitation:

(26) The data for alkyl polyacrylate identified as CO(AB-AH) wherein R.sup.1=hydrogen, R.sup.2=n-butyl, R.sup.3=hydrogen, R.sup.4=n-hexyl) are shown in Table 1, which does not mean limitation:

(27) TABLE-US-00001 TABLE 1 Number average molecular mass (Mn) and polydispersity index (I) of copolymers measured by SEC. Copolymer Mn (Daltons) I Co(AB-AH)-1 98 000 2.25 Co(AB-AH)-2 112 000 2.03

(28) The data of alkyl polyacrylate identified as CO(AH-AL) wherein R.sup.1=hydrogen, R.sup.2=n-butyl, R.sup.3=hydrogen, R.sup.4=n-lauryl) are shown in Table 2, which does not mean limitation:

(29) TABLE-US-00002 TABLE 2 Number average molecular mass (Mn) and polydispersity index (I) of copolymers measured by SEC. Polymer Mn (Daltons) I Co(AB-AL)-1 80 000 1.52 Co(AB-AL)-2 103 640 1.89

(30) The data for alkyl polyacrylate whereinR.sup.1=hydrogen, R.sup.2=n-hexyl, R.sup.3=hydrogen, R.sup.4=phenoxyethyl) identified as CO(AH-AEF) are shown in Table No. 3, which does not imply any limitation:

(31) TABLE-US-00003 TABLE 3 Number average molecular mass (Mn) and polydispersity index (I) of copolymers measured by SEC. Copolymer Mn (Daltons) I Co(AH-AEF)-1 126 100 2.45 Co(AH-AEF)-2 138 700 2.64

(32) In Table 4 is shown the results for alkyl polyacrylate wherein R.sup.1=hydrogen, R.sup.2=n-hexyl, R.sup.3=hydrogen, R.sup.4=n-octyl) identified as CO(AH-AOc), which does not mean limitation:

(33) TABLE-US-00004 TABLE 4 Number average molecular mass (Mn) and polydispersity index (I) of copolymers measured by SEC. Copolymer Mn (Daltons) I CoAH-AOc)-1 124 500 1.98 Co(AH-AOc)-2 102 340 2.06

(34) In Table No. 5 is shown the data for alkyl polyacrylate wherein R.sup.1=hydrogen, R.sup.2=n-hexyl, R.sup.3=hydrogen, R.sup.4=n-lauryl) identified as Co(AH-AL), which does not mean limitation:

(35) TABLE-US-00005 TABLE 5 Number average molecular mass (Mn) and polydispersity index (I) of copolymers measured by SEC. Copolymer Mn (Daltons) I Co(AH-AL)-1 89 700 2.83 Co(AH-AL)-2 98 800 2.64

(36) In Table No. 6 is shown the data for alkyl polyacrylate whereinR.sup.1=hydrogen, R.sup.2=n-lauryl, R.sup.3=hydrogen, R.sup.4=n-octyl) identified as Co(AL-AOc), which does not mean limitation:

(37) TABLE-US-00006 TABLE 6 Number average molecular mass (Mn) and polydispersity index (I) of copolymers measured by SEC Copolymer Mn (Daltons) I AL-AOc-1 149 700 1.93 AL-AOc-2 130 800 2.64

EXAMPLES

(38) The following examples are presented to illustrate the spectroscopic characteristic of the copolymers based on alkyl acrylate and their application as defoamer agents in gasified crude oils with API densities between 10 to 40 API. These examples should not be regarded as limiting what is claimed.

Co(AB-AH)-1

(39) I.R. n cm.sup.1: 2958, 2929, 2866, 1736, 1463, 1383, 1258, 1166.

Co(AB-AH)-2

(40) I.R. n cm.sup.1: 2960, 2931, 2864, 1735, 1464, 1384, 1259, 1167.

Co(AB-AL)-1

(41) I.R. n cm.sup.1: 2955, 2926, 2853, 1734, 1462, 1395, 1257, 1196, 716.

Co(AB-AL)-2

(42) I.R. n cm.sup.1: 2954, 2926, 2852, 1734, 1463, 1395, 1257, 1198, 714.

Co(AH-AEF)-1

(43) I.R. n cm.sup.1: 3035, 2948, 2924, 2875, 1726, 1600, 1498, 1402, 1268, 1188, 722.

Co(AH-AEF)-2

(44) I.R. n cm.sup.1: 3035, 2942, 2926, 2875, 1726, 1600, 1498, 1402, 1269, 1189, 724.

Co(AH-AOc)-1

(45) I.R. n cm.sup.1: 2961, 2931, 2854, 1736, 1467, 1391, 1253, 1185, 730.

Co(AH-AOc)-2

(46) I.R. n cm.sup.1: 2962, 2930, 2852, 1736, 1468, 1382, 1254, 1183, 730.

Co(AH-AL)-1

(47) I.R. n cm.sup.1: 2972, 2932, 2851, 1732, 1447, 1393, 1249, 1174, 729.

Co(AH-AL)-2

(48) I.R. n cm.sup.1: 2970, 2934, 2853, 1732, 1448, 1390, 1249, 1178, 729.

Co(AL-AOc)-1

(49) I.R. n cm.sup.1: 2960, 2933, 2850, 1730, 1462, 1394, 1247, 1168, 724.

Co(AL-AOc)-2

(50) I.R. n cm.sup.1: 2962, 2931, 2853, 1730, 1464, 1396, 1247, 1170, 722.
Evaluation of Polymers as Anti-Foaming Agents in Heavy Crude Oil and Super-Heavy

(51) Crude oils, used in evaluations of the defoamers, are contained in a metal stainless steel vessel with a capacity of 4 liters; oil samples were extracted from the well to the sampling conditions at 76.5 C. and a pressure of 6 kg/cm.sup.2.

(52) Copolymers based on alkyl acrylates were evaluated as foam inhibitors in gasified heavy and super-heavy crude oils, using an apparatus for measuring the foam and an assessment procedure implemented by the applicants (Mexican patent MX/a/2013/013966). The metallic vessel containing the crude oil was instrumented with a nitrogen gas supply line, heating jackets and a vent line for the crude oil, where the defoaming agents are fed. The foaming process is induced by preheating the stainless steel vessel at an external temperature in a range from 40 to 150 C., and pressurizing the system with nitrogen gas at a pressure in a range from 80 to 150 psi, remaining at these conditions for two hours before starting the test. After annealing the metal vessel, the crude oil is released using the starting line or exhaust, the defoamer is fed into the outlet pipe through a septum-type connection (diaphragm made of a material which allows entry of a needle and when being extracted can seal the pipe) by using a syringe to a desired dosage from 10 to 2000 ppm. The foam is formed due to the sudden pressure drop of the pressurized oil in the metal container with respect to external atmospheric pressure.

(53) 150 mL of crude oil are released from the metallic vessel with formed foam, being poured into a graduated glass cylinder in approximately during 20 to 40 s. The foam collapse is measured, recording the volumes registered in the graduated glass cylinder every minute for a period of 10 min. Finally, once the test is finished, the crude oil stand in the graduated cylinder until there is no more foam and the residual crude oil is measured.

(54) Gasified heavy and super-heavy crude oils were characterized as follows:

(55) TABLE-US-00007 TABLE 5 Physical and physico-chemical characterization of crude oils Property Heavy crude oil Super-heavy crude oil API 15.00 12.84 Salt content 49.54 11.48 (lbs./1000 bbl) Paraffin content 4.32 4.75 (wt %) Temperature runoff 12 3 ( C.) Kinematic viscosity 2309.52 3423.58 (mm.sup.2/s) @ 25 C. Cryoscopy MW (g/mol) 398.00 426.44 n-heptane insolubles 10.45 16.58 (wt %) SARA analysis Saturates (wt %) 6.06 10.28 Aromatics (wt %) 5.95 26.65 Resins (wt %) 71.71 45.79 Asphaltenes (wt %) 16.22 17.25

(56) Different concentrates of each copolymer were prepared, from 5 to 40 wt %, using solvents with a boiling point in the range from 35 to 200 C., wherein the solvent is dichloromethane, methanol, ethanol, isopropanol, chloroform, benzene, toluene, xylene, jet fuel, naphtha, individually or in mixtures thereof, so small volumes of solution were added in order to stablish that there is no effect of solvent on the foam breaking. The polymers based on alkyl acrylates were evaluated at concentrations in the interval from 10 to 2000 ppm based on the amount of crude oil. The influence of the polymers based on alkyl acrylates was evaluated simultaneouslyin order to stablish a comparisonwith a silicon based commercial defoamer.

(57) a. By way of demonstration, which does not imply any limitation, FIGS. 1, 2, 3, 4, 5 and 6 show the results of evaluations of Co(AB-AH)-1, Co(AB-AH)-2, Co(AB-AL)-1, Co(AB-AL)-2, Co(AH-AEF)-1, Co(AH-AEF)-2, Co(AH-AOc)-1, Co(AH-AOc)-2, Co(AH-AL)-1, Co(AH-AL)-2, Co(AL-AOc)-1 and Co(AL-AOc)-2 copolymers as antifoam agents in gasified heavy crude oil ( API=15.00), dosed at 500 ppm; however, these copolymers have been applied from 10 to 2000 ppm. The commercial silicon-based product IMP-SI-1 brings down the foam level 20 vol % faster than that of the blank at a dose of 500 ppm.

(58) FIGS. 7, 8, 9, 10, 11 and 12 show the results of the evaluations of Co(AB-AH)-1, Co(AB-AH)-2, Co(AB-AL)-1, Co(AB-AL)-2, Co(AH-AEF)-1, Co(AH-AEF)-2, Co(AH-AOc)-1, Co(AH-AOc)-2, Co(AH-AL)-1, Co(AH-AL)-2, Co(AL-AOc)-1 and CO(AL-AOc)-2 copolymers as antifoaming agents in gasified super-heavy crude oil ( API=12.84) dosed at 500 ppm; however, these copolymers have been applied from 10 to 2000 ppm. The commercial silicon-based product IMP-SI-1 decreases the foam 20 vol % faster than the blank in a dose of 500 ppm. The efficiency of the copolymer based on alkyl acrylates is compared with the blank.

(59) FIG. 1 shows that the Co(AB-AH)-1 and Co(AB-AH)-2 copolymers are efficient as foam inhibitors, regardless of the proportion of AB in respect to AH, provoking a decrease of the foam between 30 to 40 vol % faster than the blank, and even above the defoaming efficiency of the commercial silicon-based product IMP-SI-1, dosed at 500 ppm.

(60) FIG. 2 shows that the Co(AB-AL)-1 copolymer (AB/AL: 70/30 wt %), dosed at 500 ppm, is slightly more efficient as defoamer compared with the commercial silicone-based product IMP-SI-1 at same dosage, decreasing the foam level between 20 to 25 vol % faster than the blank. Regarding the Co(AB-AL)-2 copolymer (AB/AL: 30/70 wt %) dosed at 500 ppm, the foam is reduced between 5 to 10 vol % compared with the blank. Therefore, the defoaming efficiency is favored with a higher amount of AB monomer (70 wt %) in the copolymer.

(61) FIG. 3 shows that the Co(AH-AEF)-1 copolymer (AH/AEF: 70/30 wt %) is the most efficient as defoamer agent, abating the foam between 30 to 40 vol % compared with the blank. On the other hand, the Co(AH-AEF)-2 copolymer (AH/AEF: 30/70 wt %) behaves as the commercial silicone-based product IMP-SI-1 inhibiting the foam between 20 to 25 vol %, faster than the blank. Thus, increasing the amount of AH monomer, the efficiency of the copolymer as defoamer is improved.

(62) FIG. 4 shows that the Co(AH-AOc)-1 and Co(HA-AOC)-2 copolymers, regardless of the monomer ratio, both show a similar behavior as defoamer at a dose of 500 ppm, being the defoaming efficiency slightly higher than the commercial silicon-based product IMP-SI-1, abating the foam between 25 to 30 vol % relative to the blank.

(63) FIG. 5 shows that the Co(AH-AL)-1 and Co(AH-AL)-2 copolymers have a similar behavior as defoamers, regardless of the monomer ratio; however, both copolymers are slightly less efficient than the commercial silicone-based product IMP-SI-1. The copolymers show a defoaming efficiency of 15 vol %, relative to the blank. Both copolymers were dosed at 500 ppm.

(64) In FIG. 6, the Co(AL-AOc)-1 copolymer (AL/AOc: 30/70 wt %) shows a defoaming efficiency similar to the commercial silicone-based product IMP-SI-1 between 20 to 25 vol %, both dosed at 500 ppm. On the other hand, when monomers ratio was inverted, the Co(AL-Aoc)-2 copolymer (AL/AOc: 70/30 wt %) was not capable to abate the foam, giving the same performance than the blank.

(65) FIG. 7 shows that the Co(AB-AH)-1 and Co(AB-AH)-2 copolymers are efficient as foam inhibitors, regardless of the proportion of AB in respect to AH, abating the foam between 40 to 50 vol % faster than the blank, even over the defoaming efficiency of the commercial silicone-based product IMP-Si-1, both dosed at 500 ppm.

(66) FIG. 8 shows that the Co(AB-AL)-1 copolymer (AB/AL: 70/30 wt %) is more efficient to abate the foam about 25 vol %, compared with the blank, and the copolymer is slightly better than the commercial silicone-based product IMP-SI-1. The Co(AB-AL)-2 copolymer (AB/AL: 30/70 wt %) copolymer is not able to bring down the foam, behaving like the blank. A higher amount of AB monomer (70 wt %) promotes more efficiently the foam inhibition. Both copolymers were dosed at 500 ppm.

(67) FIG. 9 shows that the Co(AH-AEF)-1 copolymer (AH/AEF: 70/30 wt %) is the most efficient as defoamer, decreasing the foam between 30 to 40 vol %, compared with the blank. The Co(AH-AEF)-2 copolymer (AH/AEF: 30/70 wt %) copolymer gives a lower efficiency as foam inhibitor, abating the foam about 20 vol %, behaving as the commercial silicone-based product IMP-SI-1. A higher amount of AH monomer improves the performance as defoamer agent.

(68) FIG. 10 shows that the Co(AH-AOc)-1 copolymer (AH-AOc: 30/70 wt %) is able to abate the foam between 30 to 40 vol % relative to the blank. The Co(AH-AOc)-2 copolymer (AH/AOc: 70/30 wt %) displays a similar behavior as the commercial silicone-based product IMP-SI-1, decreasing the foam 20 vol %. Both copolymers were dosed at 500 ppm.

(69) FIG. 11 shows that the Co(AH-AL)-1 copolymer (AH/AL: 30/70 wt %) and the Co(AH-AL)-2 copolymer (AH/AL 30/70 wt %) display better efficiency as defoamer than the commercial silicone-based product IMP-SI-1, where the first one gave the best performance abating the foam between 30 to 40 vol % compared with the blank; whereas the second one reached 25 vol % of defoaming efficiency relative to the blank.

(70) In FIG. 12, the Co(AL-Aoc)-2 copolymer (AL/AOc: 30/70 wt %) showed a similar behavior compare to the commercial silicone-based product IMP-SI-1 abating the foam 20 vol % at 3 min of the assessment, both product dosed at 500 ppm. After this period of time, the efficiency of the copolymer increases about 30% in respect to the blank. On the other hand, when monomers ratio was inverted, the Co(AL-AOc)-1 copolymer (AL/AOc: 70/30 wt %) copolymer was not capable to abate the foam, giving the same performance than the blank.

(71) Mixtures of the formulations of acrylate copolymers based alkyl, which constitute the present invention and also mixtures formulations homopolymers acrylate based alkyl with these copolymers is evaluated, and as an example in the fact that it does not imply any limitation, performed the copolymer mixture of Co(AB-AH)-1 with Co(AL-AOC)-1. Similarly, the mixture of the Co(AB-AH)-1 copolymer with the HAH-2 homopolymer produced according to the method disclosed in Mexican patent application MX/a/2013/014352. These mixtures were evaluated as antifoam agents in gasified heavy and super-heavy crude oils (15.00 and 12.84 API), dosed at 500 ppm in both crude oils. These mixtures showed better performance as foam inhibitor compared with the blank between 15 to 40% more efficient.