CA1266559A

CA1266559A - Low toxicity oil composition and use thereof in drilling fluids

Info

Publication number: CA1266559A
Application number: CA000540230A
Authority: CA
Inventors: Robert William Dennis; Charles John Dye; Alan Keasey
Original assignee: BP Chemicals Ltd
Current assignee: BP Chemicals Ltd
Priority date: 1986-06-25
Filing date: 1987-06-22
Publication date: 1990-03-13
Anticipated expiration: 2007-03-13
Also published as: NO172128B; NO872623D0; NO172128C; JPS6317984A; AU594474B2; GB8615478D0; EP0254412B1; NO872623L; IN168310B; EP0254412A2; AU7463387A; US4839096A; DE3776827D1; EP0254412A3

Abstract

ABSTRACT OF THE DISCLOSURE

LOW TOXICITY OIL COMPOSITION AND USE THEREOF IN DRILLING FLUIDS

This invention relates to a base oil composition suitable for use in drilling fluids, the composition comprising an oil component with an aromatic hydrocarbon content of less than 10% w/w and a polar activator which is an ether alcohol or a mixture of ether alcohols. The polar activators used herein mitigates the problems of toxicity, shearing, stability and gelation in drilling fluids containing conventional base oils.

Description

Case 6315(2) LOW TO~ICITY OIL COM~OSITION AND USE THEREOF IN DRILLING FLUIDS

The present invention relates to base oil composition which have relatively lower toxicity than oils having relatively higher aromatic hydrocarbon content for use especially in drilling fluid formulations.
Drilling fluids generally contain as essential ingredients a base fluid component such as diesel or water, emulsifiers, surfactants or wetting agents, clays, water, chlorides of sodium and calcium, and weighting materials. The base oil component is usually either a water-based, i.e. water forms the continuous phase, or, an oil-based, i.e. oil forms the continuous phase. Normally, water is purposely added to the latter types to give oil based (water-in-oil) emulsions; these are the so-called 'invert emulsions'. The function of the drilling fluid is to (a) cool and lubricate the drill bit and drill string, (b) remove drilled solids, (c) suspend drilled cuttings and other debri~ by gelation, (d) facilitate control of surface pressures, and (e) prevent caving of formations and to shore up sides of the bore holes.
The type of drilling fluid formulation used will depend amongst others upon the conditions of drilling and the geology of the formation being drilled. In addition the properties of the drilling fluid formulation are also important. These properties include its rheology, density, viscosity, gelation characteristics, ease and~
rate of filtration, pH value, solids content and stability of the emulsion. In respect of certain down hole conditions invert emulsions are preferred.

Hitherto, the base oil component used in these drilling fluids has almost exclusively been diesel. The reason for this is that diesel is relatively inexpensive and acts quickly upon the organophilic clays present as viscosifiers in drilling fluids and accelerates the s~elling and gelation of the clay. This is a necessary mechanism to impart optimum rheology to the fluid.
However, in spite of its good performance, diesel is undesirable due to the presence of a high concen~ration (up to 25% w/w) of aromatic hydrocarbons therein, of which up to 2% are polycyclic, which are toxic. Moreover, a portion of the used drilling fluids based on diesel are usually discharged into the sea because they are retained on the rock cuttings which are difficult to clean and thereby risk pollution of the environment.
Efforts have been made to rnitigate this problem by using low toxicity oils. However such oils if used alone require prolonged shearing and/or higher levels of viscosifiers such as clays to achieve the desired initial rheology. It has been recognised that this deficiency of low toxicity oils could be mitigated by using polar activators to make up for the loss of the polar aromatic components in diesel. ~owever, such efforts have been relatively unsuccessful and the drilling industry has become resigned to the added expense of extra sheaxing or the use of up to 50% more viscosifier clay to replace diesel in drilling fluids.
It has now been found that by choosing a base oil o~ low toxicity and combining it with an appropriate polar activator, the problems of toxicity, shearing, stability, gelation etc in drilling fluids containing conventional base oils can be ' r ' mitigated.
Accordingly, the present invention provides a base oil composition suitable for use in organophilic clay containing drilling fluids, said composition comprising an oil component with an aromatic hydrocarbon content of less than 10% w/w and from 1-5%
w/w of a polar ac~ivator which is an ether alcohol or is a mixture of ether alcohols selected from one or more of butoxypropanol, isobutoxypropanol,, phenoxypropanol, phenoxypropoxy propanol and substituted derivatives thereof.
The invention also provides a drilling fluid comprising as essential ingredients: one or more organophilic clays, and a base oil composition, said base oil composition comprising: an oil component with an aromatic hydrocarbon content of less than 10%
w/w and from 1-5% w/w of a polar activator which is an ether alcohol or is a mixture of ether alcohols selected from one or more of butoxypropanol, isobutoxypropanol,, phenoxypropanol, phenoxypropoxy propanol and substituted derivatives thereof.
The oil component ln the base oil composition may be suitably kerosene, gas oils low in aromatic hydrocarbons ~also known as technical gas oil) or an oil which is derived by diluting diesel 2a .
, ,~.~

with anotler oil which is low in aromatic hydrocarbon content such that the total aromatic hydrocarbon content of the composition is less than lOX w/w. Such oils axe hereafter terrned as 'low toxicity oils'.
The polar activator used in the base oil composition of the present invention is suitably a polax e-ther alcohol i.e. an ether alcohol which has inherent polarity.
The ether alcohols (also known as "glycol ethers") used contain one or more ether linkages. The ether alcohols may be aliphatic, aromatic or mixtures of these. They are suitably derivable from organic compounds having an -OH group (e.g. alcohols or phenols) such as isobutanol or phenol and an alkylene oxide but are preferably derivable Erom an aromatic compound having -OH groups such as e.B. phenol or a phenoxy propanol and an alkylene oxide which suitably has 2-4 carbon atoms, preferably 2-3 carbon atoms e.g. ethylene oxide or propylene oxide.
Thus the ether alcohol activator can be one or more of a butoxypropanol, isobutoxypropanol, phenoxyethanol, phenoxypropanol, a pheno~ypropoxypropanol or substituted derivatives thereof such that the substituents do not adversely affect the performance of the base oil composition when used in drilling fluids.
The relative amounts of the oil component and the polar activator in the base oil composition is suitably such that i-t contains from 1-5% by weight, preferably from 1.5-3.5% w/w of the activator. --Under certain conditions aromatic ether alcohols such asphenoxypropanol have a tendency to separate out from the base oil.
This is particularly so at low temperatures. In such a case it is preferable to use the aromatic ether alcohol in conjunction with an aliphatic ethex alcohol such aY ethoxypropoxypropanol. For instance, at base oil temperatures below 15C, using a mixture of ether alcohols containing from 20-50% w/w of an aliphatic ether alcohol prevents such separation. In addition, the presence of an aliphatic ether alcohol in the mixture depresses the freezing point.
As mentioned previously, drillin~ fluids contain in addition to ~,r~

the base oil composition conventional components such as clays~
water, salts, e.g. chlorides of calcium and sodium, surfactants or emulsifiers and weighting material.
The clays used in drilling fluids containing the base oil compositions of the present invention are suitably organophilic clays. If a hydrophilic clay such as bentonite is available it is necessary to transform these into an organophilic condition e.g. by reaction with appropriate organic ammonium salts by methods well known in the art. These clays act as viscosifiers and the drilling fluid is usually prepared by mixing the conventional components with the base oil composition followed by shearing to achieve the desired rheology, i.e. a fairly low plastic viscosity (PY) and a high yield point (YP) to plastic viscosity ratio, that is YP/PV.
During preparation of a drilling fluid, a preformed base oil composition containing both the low toxicity oil component and the polar activator may be mixed with the other conventional components of such fluids such as clay, water, salts, emulsifiers etc. On the other hand the two components of the base oil composition of the present invention may be mixed separately with the other drilling fluid components during agitation or shearing. In the latter case it is preferable to first mix all the polar activator and from one-quarter to one-half of the total low toxicity oil component with the clay and other ingredients. This results in a rapid swelling and gelation of the clay within a few seconds. Thereafter the remainding three quarter~ of the low toxicity oil component can be added to the swollen gel followed by shearing to achieve a drilling fluid of desired rheology, i.e. a very high YP/PV ratio.
The use of a combination of a low toxicity oil, i.e. an oil component low (less than 10% w/w) in aromatic hydrocarbon content, and a polar activator as the base oil composition can be further enhanced by reducing the amount of emu~sifiers used in the drilling fluids. The resultant drilling fluids show a yield point cnly marginally 12ss than those using diesel as the base oil and yet retain the advantages of low toxicity and low plastic viscosity.
The base oil compositions of ehe present invention and the use ~ f ~ r- ~ ~

thereof in drilling fluids is further illustrated with reference to the followlng Examples.
Examples In order to demvnstrate the relat-ive effectiveness of alcohol ethers as polar activators, other proprietary compounds such as propylene car'oonate were also tested for comparison. The results of these tests are tabulated below:-Materials Used Base Oil Composition Boiling Range Flash Point Kinematic paraffin: P C (PMCC)Viscosity naphthene: N C at 40C
aromatic A _ cS
Low P:N:A
Toxicity 56:42:2 195-255 72 1.7 Kerosine*
Low P:N:A
Toxicity 74:23:3 210-312 109 2.5 Technical 49:42:9 218-310 100 2.9 Gas Oil*
Diesel** P:N:A
~Z:37:21 200-365 65-75 3.3 *Some variation in composition and physical properties occur due to variations in crude oil feedstock.

**Sample used was not analysed. Properties shown above are for a typical diesel oil.

Polar Activators Used _ Polar Activators Approximate Composition Phenoxypropanol (PhP) Phenoxypropoxypropanol (PhDP) Mixed Phenoxypropanol/ Essentially a mlxture of PhP!PhDP
Phenoxypropoxy propanol (95/5 w/w) Mixed Isobutoxypropanol Essentially IBP 75%, IBDP 21% and others (IBP)/isobutoxypropoxy 4%).
propanol (IBDP) Phenoxypropanol (PhP) + PhP is the activator and EDP is the Ethoxypropoxypropanol cosolvent (EDP) Acetophenone PropylenP carbonate . _ .~.f~

Materials Sources (and their role in drillin~ fluids) __ _ _ Other Standard Drilling Remarks Fluid Components Geltone II* A gel-forming organophilic clay with bentonitic structure.
Duratone H7* An oil dispersible lignitic colloid used to control the filtration of oil muds. It also aids in solids suspension and emulsification.
Calcium Chloride This is dissolved in the water phase to provide osmotic force to dehydrate water wet formations and increases the mud density.
Lime Essential to adjust pH and ensure optimum performance of the emulsifiers.
Invermul-L* Maleic-tall oil amide in kerosine solvent.
This is a water-in oil primary emulsifier.
Ezmul* ~artial amide of polyamine and fatty acid in kerosine solvent. It is a secondary emulsifier and oil-wetting agent which ensures that baryte and drilled solids do not become water-wetted.
Baryte Barium sulphate (specific gravity 4.5) is _ used as weighting agent.

*Registered Trade Mark 1. Rheolo~ Measurement The characteristics of a drilling fluid can be closely defined by quoting values for PV, YP and gel strength. Standard field and laboratory tests have been devised which are quick and practical.
Such tests only approximately reflect downhole behaviour, but ~hey serve their purpose if their l mitations are understood and if the data obtained from them are correlated with experience.
A Fann viscometer was used in this study to determine the rheology of low toxicity kerosine, low toxicity technical gas oil and diesel based drilling fluids. ~ee Section 3 below for more details.

2. Standard Drillin~ Fluid ~reparation (GeneraL Procedure) The drilling fluid base oil and polar activator, if any, were measured into the mixing vessel and agitation started using an Ystral mixer. A reduced shear rate (Variac controller setting :
lOOv) was used for all stages until the final addition of barytes.
Geltone and Duratone powders were added over a period of 30 seconds. The mixture was sheared for 10 minutes.
The calcium brine was added and shearing was continued for a further 20 minutes.
The lime, Invermul and Ezmul were added and the shearing was continued for an additional 5 minutes.
The shear rate was increased (Variac setting : 120v) and the baryte was added incrementally over one or two minutes. Finally the complete drilling fluid was sheared at the higher rate for 30 minutes. The vigorous mixing caused the drilling fiuid to heat up; the final temperature being 60 + 5C.
When circulating in the oil well, the drilling fluid is exposed to much more severe shearing through the drilling bit at downhole temperatures of 150C or more. Under these conditions, the organophilic clay will yield to provide maximum structural properties after a few circulations. For specific amounts of various components used see Tables 4 and 6 below.

Drilling Fluids - Thelr Compos~tLon and Preparation _ Stand rda Drilling Fluid Composition Quan~ities used -10 Lox toxicity oil or diesel 270 ml Polar activator (if any) 5O5 ml (5.8g for PhP; d = 1.06) 15 Geltone II 8.0g Duratone H7 8.7g Calcium brine solution 85 ml 20 (brine concentration: 463g CaC12.6H20 diluted to 500 ml H20) Lime 8.0 g 25 Xnvermul solution 20 ml (Invermul solution conc: 50%
vol in base oil)b Ezmul solution 8.0 ml 30 (Ezmul solution conc: 50%
vol in kerosine) Bary~e 330g Notes:
a. The drilling fluid composition was varied slightly in some formulations; details of divergences from the above composition are given in Table 6. This formulation is for a 12.2 pounds (weight) per gallon drilling fluid.
b. Since primary and secondary surfactants (Invermul and Ezmul) were viscous liqulds, stock solutions were prepared by diluting to 50% concentration by volume in base oil. The 50~ solutlon was then used in all drilling fluid preparations.

3. Rheolo~y~Measurements_ ith the Fann 35SA Direct Indicatin~
Viscometer This is a concentric cylinder viscometer that enables the variation of shearing stress with shear rate to be observed.
Procedure for Measurin~ Drilling Fluid RheologY
The freshly prepared drilling fluid was transferred to screw top storage jars. Experience showed that the rheological characteristics of the drilling fluid did not change significantly over a period of 3 months' storage, unless exposed to further heating or shearing.
Just prior to the viscosity measurements, the drilling fluid temperature was dropped 2 or 3 degrees below 20C. The jar was vigorously shaken to ensure fluid homogeneity. A pre-set volume of drilling fluid was then transferred to the stainless steel beaker of the Fann viscometer. Then the beaker was raised until the drilling fluid surface reached a prescribed mark on the outer cylinder of the viscometer.
Readings were taken at each of six rotation speeds at the moment when the temperature had risen to 20C, it was found that small divergences from this temperature could significantly affect the viscosity readings.
The drilling fluid was then stirred by switching to maximum rotational speed for 30 seconds. Rotation was stopped for 10 seconds, then re-started at 3 rpm and the maximum momentary reading noted. Rotation was stopped again, but this time for a period of 10 minutes. After this period at rest, the maximum deflection at 3 rpm was noted once more.

ll Calculat_on of Re!sults The following example is for a kerosine drilling fluid with no polar activator ~cf Table o):

Viscometer Viscometer Rotational Readings Speed (rpm) at 20C

Reading after 4 10 seconds rest Reading after 7 lO minutes rest _ _ Apparent Viscosity (AV) = 600 rpm readin~ = 60 = 30 cP 2 2 Plastic Viscosity (PV) - 600 rpm reading - 300 rpm reading cP = 60-33=27 Yield Point (YP) - 300 rpm reading - PV = 33-27=6 lb/100 ft2 Gel Strength = Max. deflection after lOs at rest = 4 Max. deflection after 10 mins at 7 rest Ratio of Yield Point to Plastic Viscosity - 6 - 0.22 In the data tabulated in Table 6 the following abbreviations have been used:-LTK - Low toxicity kerosine LTG0 - Low toxicity technical gas oil AV - Apparent viscosity (cP) PV - Plastic viscosity ~cP) YP - Yield point (lb/lO0 ft2) t,;~

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Drillin~ Mud Rheolo~:~es (20C) ~ _ _ Mud Run Number 23 24 . _ Base Oil LTK I.TK
~ _ Activator (% weight on Propylene Acetophenone base oil) Carbonate (2.7%) (2.7%) _ _ _ Special Features of Mud _ Shear Rate (rpm) _ _ _ 600 65 6~3 Fann 300 35 38 Viscometer 200 25 28 Readings 16 16 186 Gel Strength 4~5 6/8 Apparent vis (AV) 33 34 Derived Plastic vis (PV) 30 30 RheolBY (cP) Props.
Yield Point (YP) 5 8 (lb/100 ft2) _ Ratio YP 0.17 0.27

Claims

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:-Claims:

1. A base oil composition suitable for use in organophilic clay containing drilling fluids, said composition comprising an oil component with an aromatic hydrocarbon content of less than 10% w/w and from 1-5% w/w of a polar activator which is an ether alcohol or is a mixture of ether alcohols selected from one or more of butoxypropanol, isobutoxypropanol, phenoxypropanol, phenoxypropoxy propanol and substituted derivatives thereof.

2. A base oil composition according to claim 1 wherein the polar activator is a mixture of an aromatic ether alcohol and an aliphatic ether alcohol, the latter being present in the mixture in an amount from 20-50X w/w of the total mixture.

3. A base oil composition according to claim 1 wherein said composition comprises an oil component, an ether alcohol and one or more of clays, water, halide salts of sodium or calcium, surfactants, emulsifiers and weighting material.

4. A drilling fluid comprising as essential ingredients: one or more organophilic clays, and a base oil composition, said base oil composition comprising: an oil component with an aromatic hydrocarbon content of less than 10% w/w and from 1-5% w/w of a polar activator which is an ether alcohol or is a mixture of ether alcohols selected from one or more of butoxypropanol, isobutoxypropanol, phenoxypropanol and phenoxypropoxy propanol and substituted derivatives thereof.

5. A drilling fluid according to claim 4 wherein said fluid is prepared by initially mixing the polar activator and one quarter of the oil component of the base oil composition with the clay, allowing the mixture to swell and gel, thereafter adding the remaining three quarters of the oil component to the swollen gel and finally shearing the total mixture to form the drilling fluid.