US2004198618A1PendingUtilityA1
High stability, high lubricity, low toxicity, high biodegradability drilling fluid
Est. expiryFeb 24, 2023(expired)· nominal 20-yr term from priority
C10G 2/00C09K 8/32C10G 2/32
38
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Claims
Abstract
A drilling fluid including at least about 2 wt % olefin, at least about 5 wt % n-paraffins, and at least about 2 wt % isoparaffins, wherein the isoparaffins are substantially wholly terminal monomethyl branched is provided. A method for producing the drilling fluid, and a method for drilling a borehole using the drilling fluid are disclosed.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A base fluid comprising:
at least about 5 wt % olefins; at least about 5 wt % n-paraffins; and between about 2 and 50 wt % branched paraffins wherein substantially all of the branch groups are monomethyl and wherein the ratio of terminal monomethyl branching to internal monomethyl branching is at least about 1:1.5.
2 . The base fluid of claim 1 wherein the ratio of terminal monomethyl branching to internal monomethyl branching is at least about 1:1.
3 . The base fluid of claim 1 wherein the n-paraffins are present in an amount of at least about 20 wt % and wherein the ratio of terminal monomethyl branching to internal monomethyl branching is at least about 1.5:1.
4 . The base fluid of claim 1 wherein the n-paraffins are present in an amount of at least about 40 wt % and wherein the ratio of terminal monomethyl branching to internal monomethyl is at least about 2:1.
5 . The base fluid of claim 1 wherein the base fluid is a product of a Fischer-Tropsch reaction.
6 . The base fluid of claim 5 wherein the Fischer-Tropsch reaction incorporates feed syngas having 10-60% N 2 .
7 . A drilling fluid comprising:
the base fluid of claim 1 .
8 . The drilling fluid of claim 7 further comprising:
at least one additive selected from the group of surfactants, viscosifiers, weighting agents, fluid loss control agents and proppants.
9 . A drilling fluid comprising:
from about 2 to about 90 wt % olefins; from about 2 to about 50 wt % isoparaffins; wherein the isoparaffins are substantially terminal monomethyl branched. from about 5 to about 90 wt % n-paraffins; and from about 0 to about 10 wt % oxygenates.
10 . The drilling fluid of claim 9 wherein the olefins are present in an amount of from about 7 to about 10 wt %.
11 . The drilling fluid of claim 9 wherein the isoparaffins are present in an amount of from about 3 to about 15 wt %.
12 . The drilling fluid of claim 9 wherein the n-paraffins are present in an amount of from about 65 to about 90 wt %.
13 . The drilling fluid of claim 9 wherein the oxygenates are present in an amount of from about 0 to about 5 wt %.
14 . The drilling fluid of claim 9 wherein the base fluid is a product of Fischer-Tropsch reaction on a synthesis gas.
15 . The drilling fluid of claim 14 wherein the Fischer-Tropsch reaction incorporates feed syngas having 10-60% N 2 .
16 . The drilling fluid of clam 14 wherein the synthesis gas is produced by autothermal reformation.
17 . The drilling fluid of claim 16 wherein the autothermal reformation occurs in the presence of air.
18 . The drilling fluid of claim 16 wherein the autothermal reformation occurs in the presence of 10-60% N 2 .
19 . The drilling fluid of claim 9 further comprising:
at least one additive selected from the group of surfactants, viscosifiers, weighting agents, fluid loss control agents and proppants.
20 . The drilling fluid of claim 9 wherein the olefins are:
from about 7 to about 10 wt %;
the isoparaffins are from about 2 to about 15 wt %; wherein the isoparaffins are substantially terminal monomethyl branched.
The n-paraffins are from about 65 to about 90 wt %; and
the oxygenates are from about 0 to about 5 wt %.
21 . The drilling fluid of claim 20 wherein the drilling fluid is a product of a Fischer-Tropsch reaction.
22 . The drilling fluid of claim 20 further comprising:
at least one additive selected from the group of surfactants, viscosifiers, weighting agents, fluid loss control agents and proppants.
23 . The drilling fluid of claim 20 wherein the base fluid comprises from about 25 to about 85 volume % of the drilling fluid.
24 . The drilling fluid of claim 23 wherein the base fluid comprises from about 25 to about 85 volume % of the drilling fluid.
25 . The drilling fluid of claim 22 wherein the Fischer-Tropsch reaction incorporates feed syngas having 10-60% N 2 .
26 . The drilling fluid of claim 23 wherein the feed syngas is produced by autothermal reformation in the presence of air.
27 . A process for producing a drilling fluid comprising the steps of:
(a) producing a light Fischer-Tropsch liquid; (b) distilling the light Fischer-Tropsch liquid to obtain a C 13 -C 20+ product having C 13 -C 20+ hydrocarbons and oxygenates. (c) dehydrating all or a part of the alcohols in the C 13 -C 20+ product by passing the C 13 -C 20+ product over an activated alumina catalyst to produce a dehydrated product; (d) recovering the dehydrated product; and (e) separating the aqueous and organic phases of the dehydrated product.
28 . The process of claim 27 further comprising the step of:
(f) adding one or more additive selected from the group of surfactants, viscosifiers, weighting agents, fluid loss control agents and proppants to the organic phase of the dehydrated product.
29 . The process of claim 27 further comprising the step of (b 1 ) vaporizing the C 13 -C 20+ product before step (c) and after step (b).
30 . The process of claim 29 wherein the dehydrated product from step (c) is in the gaseous state and step (d) further includes condensing the dehydrated product.
31 . The process of claim 30 wherein the heat from condensing the dehydrated product is recycled to at least partially vaporize the C 13 -C 20+ product in step (b 1 ).
32 . The process of claim 27 wherein the light Fischer-Tropsch liquid is produced from a feed syngas having 10-60% N 2 .
33 . The process of claim 27 wherein the feed syngas is produced by autothermal reformation in the presence of air.
34 . The process of claim 27 wherein a C 14 -C 18 product is obtained in step (b) and dehydrated in step (c).
35 . A method of drilling a borehole in a subterranean formation comprising the steps of:
(a) rotating a drill bit at the bottom of the borehole; (b) introducing a drilling fluid into the borehole wherein the drilling fluid comprises a base fluid comprising:
from about 5 to about 90 wt % olefins;
from about 2 to about 50 wt % isoparaffins; wherein the isoparaffins are substantially terminal monomethyl branched;
from about 5 to about 90 wt % n-paraffins; and
from about 0 to about 10 wt % oxygenates.
36 . The process of claim 35 wherein the drilling fluid comprises:
from about 7 to about 10 wt % olefins;
from about 2 to about 15 wt % isoparaffins; wherein the isoparaffins are substantially terminal monomethyl branched;
from about 65 to about 90 wt % n-paraffins; and
from about 0 to about 5 wt % oxygenates.
37 . The process of claim 35 wherein the base fluid is derived from a Fischer-Tropsch reaction.
38 . The process of claim 37 wherein the Fischer-Tropsch reaction incorporates feed syngas having 10-60% N 2 .
39 . The process of claim 37 wherein the feed syngas is produced by autothermal reformation in the presence of air.Join the waitlist — get patent alerts
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