DRILLING FLUID COMPOSITION COMPRISING VEGETABLE DERIVATIVES

Abstract

A drilling fluid composition comprising a continuous phase and a disperse phase, the continuous phase comprising fatty acid methyl esters derived from soy oil, and sunflower lecithin as an emulsifier. A method for increasing the electrical stability of a drilling fluid composition.

Claims

1. A drilling fluid composition comprising a continuous phase and a disperse phase, the continuous phase comprising fatty acid methyl esters derived from soy oil, and sunflower lecithin as an emulsifier.

2. The composition of claim 1, further comprising one or more additives selected from a viscosifier a rheology modifier, a filtration reducer and a densifier.

3. The composition of claim 1, further comprising an organophilic clay as a viscosifier, a fatty acid amide as a rheology modified, gilsonite as a filtration reducer and baryte as a densifier.

4. The composition of claim 1, wherein the disperse phase comprises a brine solution comprising 20% CaC12 in weight.

5. The composition of claim 1, wherein the emulsifier is at a concentration of about 4% to about 6% in volume.

6. The composition of claim 5, wherein the emulsifier is at a concentration of about 5% in volume.

7. The composition of claim 1, wherein the emulsifier is at a concentration of about 0.5 % to about 3% (v/v).

8. A method for increasing the electrical stability of a drilling fluid composition comprising a continuous phase and a disperse phase, the continuous phase comprising fatty acid methyl esters derived from soy oil, the method comprising adding sunflower lecithin as an emulsifier to reach a concentration of about 4% to about 6% in volume.

9. The method according to claim 8, wherein the emulsifier is added to reach a concentration of about 5% in volume.

10. A method for increasing the electrical stability of a drilling fluid composition comprising a continuous phase and a disperse phase, the continuous phase comprising fatty acid methyl esters derived from soy oil, the method comprising adding sunflower lecithin as an emulsifier to reach a concentration of about 0.5% to about 3% in volume.

Description

DETAILED DESCRIPTION

[0015] The invention will be described in further detail below.

[0016] As used herein, the term “fuel oil”, or interchangeably “gasoil”, relates to a fraction obtained by petroleum distillation, comprising distillates and residues, consisting essentially of long-chain hydrocarbons, namely alkanes, cycloalkanes, and aromatics.

[0017] The term “fatty acid methyl ester (FAME)” as used herein refers to fatty esters derived from transesterification of triglycerides with methanol. In the context of the invention FAME refers to esters derived from triglycerides of vegetable origin, such as vegetable oil. These compounds are comprised in the “vegetable base” that is used in the drilling fluid compositions of the present invention, and which differs from the fuel oil used in traditional drilling fluid compositions of OBMs. Non-limiting examples of the vegetable oils that may be used to prepare the vegetable base by transesterification include soy oil, sunflower oil, canola oil, palm oil, cottonseed oil and Jatropha oil. Preferred embodiments of the drilling fluid compositions provided by the invention use FAMEs derived from soy oil.

[0018] The inventors found that certain n-alkyl carboxylate compounds, such as sunflower lecithin, can be successfully employed to formulate drilling muds, when used emulsifiers for an oil-in-water (O/W) emulsion. Surprisingly, the formulated drilling muds display properties equivalent to those of conventional OBMs, such us density, rheological properties, electrical stability, retort and HPHT filtrate values.

[0019] Sunflower lecithin is a commercially available vegetable derivative employed as an emulsifier in several technology fields, such as the food and cosmetic industries. This compound presents a low solubility in water, but in an aqueous solution, such as an oil-in-water solution, phospholipids may form micelles, resulting in an amphiphilic surfactant.

[0020] By using lecithin or other n-alkyl carboxylates as an emulsifier, the use of strong bases such as calcium or sodium hydroxide is advantageously avoided, since there is no need for activating the emulsifier. The use of strong bases in the presence of the triglycerides of the FAME results in saponification reactions, which hinder the product application when subjected to high temperatures.

[0021] The adequate vegetable base for the drilling fluid composition may be selected according to methods known in the art, such as by determining the Equivalent Alkane Carbon Number (EACN). This dimensionless number is a parameter related to the hydrophobicity of the vegetable base and reflect the ability of these fatty acid molecules to penetrate the interfacial film.

[0022] The EACN may be measured using commercially available equipment, such as a SITE100 spinning drop tensiometer as provided by Krüss.

[0023] The value of the EACN obtained is subsequently correlated to an emulsifier concentration using empirical correlations, in order to determine which emulsifiers are suitable for a given FAME composition at specific emulsion composition and temperature conditions.

[0024] As a first step, an emulsion comprising a FAME base and brine solution at 20% (w/w) CaCl.sub.2 was assessed at 40° C., resulting in the following suitable emulsifiers: [0025] Ionic emulsifiers: [0026] Isoalkyl phenols, C.sub.12 to C.sub.14 [0027] N-alkyl carboxylate C.sub.16 [0028] N-alkyl sulfonate C.sub.20 [0029] Non-ionic emulsifiers: [0030] Surfactants between sorbitan monolaurate (Span 20) and polysorbates such as Tween 85

[0031] As a second step, temperatures of 105° C. were evaluated, representative of the conditions to which a drilling fluid is subjected. For these conditions, isoalkyl phenols, C.sub.18 to C.sub.20 were found to be suitable ionic emulsifiers.

[0032] According to these results, a n-alkyl carboxylate would not be an adequate emulsifier for conditions with a temperature of about 105° C. Surprisingly, as shown in the examples below, the inventors found that a chemical compound of the n-alkyl carboxylate family, i.e. sunflower lecithin, displayed adequate emulsifying properties at both 40° C. as well as 105° C., even though this compound does not belong to any of the emulsifier families detected for 105° C.

[0033] This fact may indicate that the properties of the emulsifiers identified for 40° C. are not significantly altered by the temperature conditions, when used in a drilling fluid comprising commonly employed additives in addition to the emulsifier.

EXAMPLES

Formulation of a FAME-Based Drilling Fluid Using Sunflower Lecithin

[0034] A drilling mud composition was formulated in order to assess its rheological properties, as compared to those of an OBM.

[0035] The vegetable-derived, i.e. FAME-based, drilling fluid was tested before and after an aging process, carried out at 105° C. during 16 h in a roller oven.

[0036] In order to adequately compare the relevant physical properties of both the FAME-based formulation of the invention and the OBM, a rheology modifier (Fatty Acid Amide), a filtration reducer (Gilsonite) and a densifier (Baryte) were included in both formulations. An organophilic clay was used as a viscosifier.

[0037] The formulations for both drilling fluids are shown in Tables 1 and 2 below:

TABLE-US-00001 Formulation for a FAME-based fluid of the invention FAME-based fluid Units Amount FAME L/m.sup.3 617 Organophilic clay kg/m.sup.3 5 Sunflower lecithin L/m.sup.3 9 Calcium Chloride Kg/m3 49 Water L/m.sup.3 265 Fatty Acid Amide L/m.sup.3 3 Gilsonite kg/m.sup.3 16 Baryte kg/m.sup.3 361

TABLE-US-00002 Formulation for an OBM OBM Units Amount Fuel oil L/m.sup.3 685 Organophilic clay kg/m.sup.3 16 Primary emulsifier L/m.sup.3 2 Secondary emulsifier L/m.sup.3 10 Calcium hydroxide kg/m.sup.3 10 Brine (CaCl.sub.2, 20% w/w) L/m.sup.3 187 Fatty Acid Amide L/m.sup.3 3 Gilsonite kg/m.sup.3 8 Baryte kg/m.sup.3 402

[0038] The following tests were carried out for each of the formulations following the standard API RP 13B-2: viscosity, plastic viscosity, yield point, gel, high-pressure, high-temperature (HTPT) filtration.

[0039] The volumetric compositions of each phase (O, W and S for the solid fraction) were determined using the retort test of standard API RP 13B-2.

[0040] Experimental results for both drilling fluids, both before and after the aging process, are shown in Table 3 below. Viscosity results indicate the reading on a OFITE’s model 900 rotational viscometer.

TABLE-US-00003 Measured properties for a FAME-based fluid of the invention and an OBM Property Units FAME-based fluid OBM Before aging After aging Before aging After aging Density g/L 1240 1240 1210 1210 Electrical stability V 161 328 671 1052 Viscosity 600 rpm DR 52 45 32.4 28.3 Viscosity 300 rpm DR 31 25 18.2 15.8 Viscosity 200 rpm DR 24 17 11.9 10.1 Viscosity 100 rpm DR 17 11 7.4 6 Viscosity 6 rpm DR 9,2 5,4 2.9 2.5 Viscosity 3 rpm DR 8,2 5,1 2.7 2.4 Plastic viscosity cP 21 20 14.159 12.497 Yield point lb/100 ft.sup.2 10 5 4.3388 3.5337 Gel 10 seconds lb/100 ft.sup.2 9 5 3 3 Gel 10 minutos lb/100 ft.sup.2 9 5 4 5 HPHT filtration @ 225° F. / 500 dpsi ml 4 5 3.6 2.8 %S %v 21,4 21,4 13 16 % W %v 24 24 19 17.5 % O %v 54,6 54,6 68 66.5 Ratio O/W %v 70/30 70/30 78.2/21.8 79.17/20.83

[0041] The experiment results show that FAME-based fluids of the invention have adequate properties, i.e. density, rheological properties and filter values for their use as drilling fluids compared to traditional OBMs.