Patent Application
20150218433
During drilling operations for oil and gas explorations, a drilling fluid or mud is typically circulated through the wellbore to facilitate the drilling process. This shortens the drilling time by lubricating the rotary drill bits that are located at the end of drill pipe string, and also by lubricating the drill pipe string that can stick or rub against the borehole causing undesirable increased friction, energy loss, misdirection of the drilling, and eventually slowing down the drilling process. The drilling mud is also designed to carry out cuttings or debris generated by drilling and to stabilize the well bore formation, preventing it from collapsing by its hydrostatic pressure exerted on the well-bore walls to maintain their integrity.
Drilling muds can be categorized according to their base: water-based muds (WBM) or oil-based muds (OBM). WBM typically include bentonite clay or polymeric (solids-free) thickeners to suspend or thicken the aqueous continuous phase which can be derived from fresh water or salt solutions (or brines) as in brine muds (BRM). OBM or invert-emulsion water-in-oil mud consist of 50:50 to 95:5 blend ratios of oil to water in which oil is the continuous phase. The continuous hydrocarbon phase in OBM can be diesel, mineral oil, natural vegetable oils, synthetic esters, or olefins.
In addition to their respective base, the commonly used components of both WBM and OBM include:
Some exemplary publications dealing with the use of fatty esters as the lubricant in drilling muds are illustrated in U.S. Pat. Nos. 4,964,615; 5,318,956; and 5,618,780; as well as in published United States Patent Application No. 2010/0305009 A1; and also in published PCT Patent Application No. WO 2011/019722 A2. The teachings of these publications are hereby incorporated by reference.
A drilling-fluid composition having an oil-based mud, water-based mud, or synthetic-based mud; and a fluid lubricant having a pour point ranging from −5° C. to −30° C., the fluid lubricant having a sulfurized fatty ester, a sulfurized olefin, or a combination thereof, wherein the sulfurized fatty ester is 5 to 15% by weight sulfur and selected from the group consisting of sulfurized biodiesel; sulfurized methyl oleate, and sulfurized methyl esters derived from vegetable oil, wherein the sulfurized olefin is 5 to 15% by weight sulfur and selected from the group consisting of sulfurized alpha or internal olefins ranging from C8 to C18; and the fluid lubricant being present in the composition in an amount ranging from 0.1 to 10% by weight.
A drilling-fluid composition having a fluid lubricant having a pour point ranging from −5° C. to −30° C., the fluid lubricant having a sulfurized fatty ester, a sulfurized olefin, or a combination thereof, wherein the sulfurized fatty ester is 5 to 15% by weight sulfur and selected from the group consisting of sulfurized biodiesel; sulfurized methyl oleate, and sulfurized methyl esters derived from vegetable oil, and wherein the sulfurized olefin is 5 to 15% by weight sulfur and selected from the group consisting of sulfurized alpha or internal olefins ranging from C8 to C18.
A subterranean-drilling method having the steps of performing subterranean drilling using a fluid lubricant having a pour point ranging from −5° C. to −30° C., the fluid lubricant having a sulfurized fatty ester, a sulfurized olefin, or a combination thereof, wherein the sulfurized fatty ester is 5 to 15% by weight sulfur and selected from the group consisting of sulfurized biodiesel; sulfurized methyl oleate, and sulfurized methyl esters derived from vegetable oil, wherein the sulfurized olefin is 5 to 15% by weight sulfur and selected from the group consisting of sulfurized alpha or internal olefins ranging from C8 to C18.
The examples and following embodiments are illustrative only and not meant to limit the inventive embodiments.
In embodiments, the fluid lubricant can be used at 0.1-10 wt % based on total weight of drilling fluids. In the experimental work described herein, the drilling fluids are tested at approximately 1 weight percent (wt %).
In embodiments, the sulfurized fatty ester illustrated in this invention is 10% S sulfurized biodiesel or methyl oleate or methyl esters derived from vegetable oils.
In embodiments, fatty esters that can be used to generate the novel lubricant additives of the topic of this invention can be any fatty esters such as all condensation products between polyols and carboxylic acids which include all well-known fatty acids such as stearic acid, lauric acid, oleic acid, linoleic acid, ricinoleic acid, dimer acid, and tall oil fatty acid.
In embodiments, olefins that can be used to generate the novel lubricant additives of the topic of this invention can be any alpha or internal olefins ranging from C8 to C24, can be branched or linear or blends thereof.
Blends of the above-mentioned fatty esters and olefins can be used to generate fluid-lubricant embodiments; and often it is the necessity to utilize such a blend of fatty esters and olefins to achieve a minus −20 C pour point that is the minimal pour point for the novel sulfurized lubricants to be poured out from the drums during the winter months in north Dakota, Ohio, or Pennsylvania.
In embodiments, the standard sulfurization process can be described ad follows: 10% sulfur flour is charged along with 90% fatty esters or olefins, or their blends into the 4-necked round bottom flask which is equipped with a thermometer, a nitrogen sparger, a mechanical stirrer, and a off-gas outlet which leads to the caustic solution scrubber. The reaction temperature is slowly raised to 165 C and an exotherm will take place to push the reacting temperature to 185-200 C. Allow the batch to cool down to 175 C, cook for two more hours, then cool the batch to 100 C before air blowing for two hours.
10.0 g sulfur flour and 90.0 g biodiesel or methyl esters of vegetable oils are allowed to react according to the standard sulfurization which is described in the last full paragraph of immediately above page 4.
10.0 g sulfur flour and 90.0 g 1-dodecene or C12 alpha olefin are allowed to react according to the standard sulfurization which is described in the last full paragraph of immediately above page 4.
10.0 g sulfur flour, 54.0 g 1-decene or alpha C10 olefin, and 36.0 g biodiesel or methyl esters of vegetable oils are allowed to react according to the standard sulfurization which is described in the last full paragraph of immediately above page 4.
10.0 g sulfur flour, 54.0 g 2-nonene, and 36.0 g biodiesel or methyl esters of vegetable oils are allowed to react according to the standard sulfurization which is described in the last full paragraph of immediately above page 4.
The oil-based drilling fluid or oil-based mud (OBM) used in illustrated the usefulness and novelty of the patentable lubricant is a fresh sample of a commercial product made with diesel as its base carrier.
The synthetic-based drilling fluid or synthetic-based mud (SBM) used in illustrated the usefulness and novelty of the patentable lubricant is a fresh sample of a commercial product made with synthetic oligomers or polymers of short chained olefins as its base carrier.
The SBM drilling fluids are more and more acceptable and preferred over its OBM or diesel counterpart due to the increasing environmental concerns over the toxicity and biodegradability of spilled muds into waterways and environment which surround oil rigs.
The friction or friction reduction in percents of all experimental drilling muds as prepared by the above Table I were measured using an EP/lubricity tester such as Fann EP/Lubricity Tester which is the standard instrument in the field of oil and gas exploration. During this test, a hardened steel block rubs against a steel O-ring or cup while being submerged in the tested drilling fluid. A load is applied on the steel block transmitting to the steel ring by applying a constant load of 150 lbs using a lever arm which “squeezes” the steel block and the steel cup that rotates at the speed of 60 rpm. The torque in lb-in was recorded on a digital dial, and friction reduction was calculated based on the torques obtained with a blank mud which contains no lubricant and the one obtained with the same mud containing 2% of the novel lubricants. The generated data supporting a basis for the novelty of this invention is tabulated below in Table III.
Thus, the novel lubricants did demonstrate strongly their friction reduction capabilities in various types of drilling fluids and below −20 C pour points.
The examples are illustrative only and not meant to limit the invention, as measured by the scope and merit of the claims. The invention has been described with reference to preferred and alternate embodiments. Modifications and alterations will occur to others upon the reading and understanding of the specification. It is intended to include all such modifications and alterations insofar as they come within the scope of the appended claims or the equivalents thereof.
This utility patent application claims priority to U.S. provisional patent application Ser. No. 61/935,446 having a filing date of Feb. 4, 2014. The provisional patent application's subject matter is hereby incorporated by reference into this application.
| Number | Date | Country | |
|---|---|---|---|
| 61935446 | Feb 2014 | US |
