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Patent 3023705 Summary

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(12) Patent: (11) CA 3023705
(54) English Title: NOVEL SYNTHETIC CAUSTIC COMPOSITION
(54) French Title: NOUVELLE COMPOSITION CAUSTIQUE SYNTHETIQUE
Status: Granted and Issued
Bibliographic Data
(51) International Patent Classification (IPC):
  • C09K 3/00 (2006.01)
  • C02F 1/66 (2006.01)
  • C09K 8/03 (2006.01)
  • C09K 8/68 (2006.01)
  • C09K 8/80 (2006.01)
  • C10G 19/02 (2006.01)
(72) Inventors :
  • PURDY, CLAY (Canada)
  • WEISSENBERGER, MARKUS (Canada)
(73) Owners :
  • DORF KETAL CHEMICALS FZE
(71) Applicants :
  • DORF KETAL CHEMICALS FZE (United Arab Emirates)
(74) Agent: BURNET, DUCKWORTH & PALMER LLP
(74) Associate agent:
(45) Issued: 2023-08-29
(22) Filed Date: 2018-11-09
(41) Open to Public Inspection: 2020-05-09
Examination requested: 2021-05-12
Availability of licence: N/A
Dedicated to the Public: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data: None

Abstracts

English Abstract

An aqueous caustic composition comprising: a caustic component; an amino acid additive adapted to provide an extended buffering effect to the caustic composition when such is exposed to an acid; and water, wherein the caustic component and the amino acid additive are present in a molar ratio ranging from 15:1 to 5:1. Methods of using such compositions are also disclosed.


French Abstract

Il est décrit une composition caustique aqueuse comprenant un composant caustique; un additif acide aminé conçu pour fournir un effet tampon étendu à la composition caustique lorsqu'elle est exposée à un acide; et de l'eau, le constituant caustique et l'additif acide aminé étant présents selon un rapport molaire situé dans la plage allant de 15:1 à 5:1. Il est également décrit des procédés d'utilisation de telles compositions.

Claims

Note: Claims are shown in the official language in which they were submitted.


CLAIMS
1. An aqueous caustic composition consisting of:
- a caustic component present in a concentration ranging from 5 wt % to 40 wt
% of the aqueous
caustic composition;
- an amino acid additive present in a concentration ranging from 2 wt % to 25
wt % of the
aqueous caustic composition, wherein the amino acid additive is adapted to
provide an extended
buffering effect to the aqueous caustic composition when such is exposed to an
acid; and
water;
wherein the amino acid additive is selected from the group consisting of:
alanine; arginine; asparagine; aspartic
acid; cysteine; glutamic acid; glutamine; histidine; isoleucine; leucine;
lysine; methionine; phenylalanine;
proline; serine; threonine; tryptophan; tyrosine; valine; and salts thereof,
and
wherein the amino acid additive buffers a pH of the aqueous caustic
composition between 8.25 and 10.
2. The aqueous caustic composition according to claim 1, wherein the
caustic component is selected from
the group consisting of: potassium hydroxide; sodium hydroxide; and
combinations thereof.
3. The aqueous caustic composition according to claim 1, wherein the amino
acid additive is selected from
the group consisting of: lysine monohydrochloride; threonine; and methionine.
4. The aqueous caustic composition according to claim 1, wherein the
caustic component is present in a
concentration ranging from 10 wt% to 30 wt % of the aqueous caustic
composition.
5. The aqueous caustic composition according to claim 1, wherein the
caustic component is present in a
concentration ranging from 15 wt% to 25 wt % of the aqueous caustic
composition.
6. The aqueous caustic composition according to claim 1, wherein the
caustic component is present in a
concentration of approximately 25 wt % of the aqueous caustic composition.
7. The aqueous caustic composition according to claim 1, wherein the amino
acid additive is present in a
concentration ranging from 4 wt % to 15 wt % of the aqueous caustic
composition.
8. The aqueous caustic composition according to claim 1, wherein the amino
acid additive is present in a
concentration ranging from 4 wt % to 10 wt % of the aqueous caustic
composition.
16

9. The aqueous caustic composition according to claim 1, wherein the
aqueous caustic composition has a
freezing point of less than ¨18 C.
10. The aqueous caustic composition according to claim 1, wherein the amino
acid additive is lysine
monohydrochloride and wherein the aqueous caustic composition has a freezing
point of about ¨45 C.
11. The aqueous caustic composition according to claim 1, where the caustic
component and the amino acid
additive are present in a molar ratio ranging from 15:1 to 5:1.
12. The aqueous caustic composition according to claim 1, wherein the amino
acid additive is selected from
the group consisting of lysine monohydrochloride, threonine, and methionine,
wherein the caustic component is
one or more of potassium hydroxide and sodium hydroxide.
13. A fracturing fluid comprising a crosslinked polymer and the aqueous
caustic composition according
to claim 1.
14. The fracturing fluid according to claim 13, wherein the crosslinked
polymer is a borate or zirconate
crosslinked guar gum polymer.
15. The fracturing fluid according to claim 13, wherein the crosslinked
polymer comprises a polymer
selected from the group consisting of a guar gum, a carboxymethyl guar gum, a
hydroxymethyl guar gum, a
hydroxypropylethyl guar gum, an o-carboxymethyl-o-hydroxypropyl guar gum, an
ammonium hydroxyl propyl
trimethyl chloride of guar gum, an o-carboyxymethyl-o-2 hydroxy-3-
(trimethylammonia propyl) guar gum, an
acryloyloxy guar gum, a methacryloyl guar gum, a hydroxy propyl guar, a
carboxy methyl guar, a carboxy
methyl hydroxy propyl guar, and guar.
16. An aqueous caustic composition consisting of:
- a caustic component;
- an amino acid additive adapted to provide an extended buffering effect to
the aqueous caustic
composition when such is exposed to an acid, wherein the amino acid additive
buffers a pH of the
aqueous caustic composition between 8.25 and 10; and
- water;
17

wherein the amino acid additive is selected from the group consisting of:
alanine; arginine; asparagine; aspartic
acid; cysteine; glutamic acid; glutamine; histidine; isoleucine; leucine;
lysine; methionine; phenylalanine;
proline; serine; threonine; tryptophan; tyrosine; valine; and salts thereof,
and
wherein the caustic component is present in a concentration of up to 40 wt %
of the aqueous caustic composition
and the caustic component and the amino acid additive are present in a molar
ratio ranging from 15:1 to 5:1.
17. The aqueous caustic composition according to claim 16, where the
caustic component and the amino
acid additive are present in a molar ratio ranging from 12:1 to 8:1.
18. The aqueous caustic composition according to claim 16, wherein the
caustic component comprises
hydroxide anion and a monovalent cation.
19. The aqueous caustic composition according to claim 16, wherein the
aqueous caustic composition has
a freezing point of less than ¨18 C.
20. The aqueous caustic composition according to claim 16, wherein the
amino acid additive is selected
from the group consisting of lysine monohydrochloride, threonine, and
methionine, wherein the caustic
component is one or more of potassium hydroxide and sodium hydroxide.
18

Description

Note: Descriptions are shown in the official language in which they were submitted.


NOVEL SYNTHETIC CAUSTIC COMPOSITION
FIELD OF THE INVENTION
The present invention is directed to a novel synthetic caustic composition,
more specifically a novel
composition comprising a caustic component and an additive adapted to provide
an extended and linear
buffering effect.
BACKGROUND OF THE INVENTION
Caustic compositions have a wide variety of uses in the oil and gas industry.
They can be used for
pH control in aqueous solutions as well as to control alkalinity. Caustic
compositions also find other varied
uses which includes, among others, breaking down of organic matter and
removing various impurities in
the refining stage of petroleum production. The impurities it can be most
effectively used to remove include
carbon dioxide and various sulfur-containing compounds. Removal of sulfur-
containing compounds is also
referred to in the industry as sweetening the petroleum. Some hydroxides can
be highly hazardous materials
to handle because they are very hygroscopic and typically have a high
exothermic reaction with other fluids,
especially low pH fluids. Sodium hydroxide is soluble in water, ethanol and
methanol. These solutions
can cause severe, irreversible dermal/ocular burns. Sodium hydroxide may cause
chemical conjunctivitis
and corneal damage. Severe eye burns with clouding of the surface, and ensuing
blindness may occur from
exposure to liquid sodium hydroxide. Low concentration levels of mists or
aerosols cause burning
discomfort, spasmodic blinking or involuntary closing of the eyelids, redness,
and tearing. At room
temperature sodium hydroxide is a white crystalline, odorless, deliquescent
solid, which absorbs moisture
from the air. When sodium hydroxide is dissolved in water, often a mist is
formed. Sodium hydroxide
itself is nonflammable, but in contact with moisture it may ignite
combustibles. Toxic fumes may be formed
upon heating. The solid, solutions, mists, and aerosols are all corrosive.
Sodium hydroxide (widely utilized) is available commercially in a solid
(sodium hydroxide is most
commonly sold as flakes, prills, and cast blocks) or a liquid solution
(normally a 50% strength). Typically,
in an oil & gas drilling application a solid bead or flake is added to a
mixing barrel with water until
solubilized and then added to the mud system or fluid system to increase the
pH for various reasons, such
as to limit the precipitation of calcium and magnesium from a hard water
source, limit the incompatibility
of the fluid system with formation clays/shales and reduce swelling. Another
advantage of a liquid sodium
hydroxide is the absorption of hydrogen sulfide and carbon dioxide gases from
a fluid system. Having an
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alternative product that is lower-hazard and more environmentally responsible
is advantageous due to the
high level of human exposure, and the fact that drill cuttings (that have
residuals of the mud system) are
often spread over agricultural fields as a disposal technique.
A 25 to 50% sodium hydroxide solution is widely utilized in the bitumen
extraction process with
relation to oil-sands development. Most commercial mineable oil sands
producers use an extraction method
"Clarks Hot Water Extraction" process which was developed in the 1920s. One of
the major operational
disadvantages of a 50% sodium hydroxide solution is that it begins to freeze
at 14 degrees Celsius and a
25% solution will freeze at -17 Celsius. It is therefore advantageous to have
a product with a much lower
freeze point, as low as -45 Celsius. As the waste fluids are intentional or
unintentionally released into the
environment post treatment, having a product that is more environmentally
responsible, low-toxicity and
lower-hazard to handle is highly advantageous. Volumes in excess of 200,000
gallons/day are utilized in
the Canadian Oil Sands, and the technical and environmental advantages for a
product with these
constituents are substantial.
Alkaline Surfactant Polymer (ASP) flood applications utilize a high pH fluid
to aid in reservoir
recovery. Having a product that is non-hazardous is an advantage. ASP
formulation typically consists of
about 0.5-1% alkali, 0.1% surfactant and 0.1% polymer. The alkaline component
reacts with the acidic
moieties that exist in the oil creating natural soap and also helps reduce the
adsorption of the surfactant on
the rock.
Borate crosslinked gel fracturing fluids utilize borate ions to crosslink the
hydrated polymers and
provide increased viscosity. The polymers most often used in these fluids are
guar and HPG. The crosslink
obtained by using borate is reversible and is triggered by altering the pH of
the fluid system (increasing the
pH generates the crosslink function, decreasing the pH eliminates the
crosslink). The reversible
characteristic of the crosslink in borate fluids helps them clean up more
effectively, resulting in good
regained permeability and conductivity.
Some of the major challenges faced in the oil & gas industry with respect to
the use of conventional
hydroxides include the following: high levels of corrosion on certain metals
which are typically countered
by the use of High Density Polyurethane (HDPE) components, intensive and
expensive maintenance
schedules - environment and equipment; reactions between hydroxides and
various types of metals can vary
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greatly but with certain metals, such as aluminum, effects are substantial
causing immediate damage. As
= caustics are utilized to control pH levels in many systems throughout the
life cycle of a well, exposure to
these metals can happen often resulting in substantial replacement costs. This
renders typical hydroxide
blends as controlled in most jurisdictions and require extensive
labeling/handling and transportation
procedures which can add to the end user's costs. Additionally, the high
toxicity levels of hydroxides render
them banned in many offshore operations due to concerns over unintentional
release into sensitive ocean
ecosystems.
= Like other highly corrosive alkalis, sodium hydroxide solutions can
decompose proteins and lipids
in skin, eyes or other living tissues via amide hydrolysis and ester
hydrolysis, which consequently causes
chemical burns and may induce permanent blindness if it contacts eye tissue.
Solid alkali may also express
its corrosive nature if there is water present on the skin or in the eyes.
Sodium hydroxide is corrosive to
several metals, like aluminum which reacts with the alkali to produce
flammable hydrogen gas on contact.
Having an alternative that is much less corrosive to metals, has a far lower
freeze point, has a linear pH
control effect and provides a period of human dermal tissue protection is
advantageous. Having one of
= those advantages is desirable, having more than one is even more so.
The inherent environmental effects (organic sterility, poisoning of wildlife
etc.) of caustics in the
event of an unintended/accidental release on surface or downhole into water
aquifers or sources of water
are devastating which can cause significant pH increase of such and can
substantially increase the toxicity
and could potentially cause a mass culling of aquatic species and potential
poisoning of humans/livestock
and wildlife exposed to/or drinking the water. An unintended release at
surface can also cause damaging
= fumes to be released, potentially endangering human and animal health.
This is a common event at large
storage sites when tanks split or leak. Typically, if near the public, large
areas need to be evacuated post
event.
The inability for many caustics and blends of such to biodegrade naturally
without irreversibly
damaging the soil, results in expensive cleanup-reclamation costs for the
operator should an unintended
release occur. Moreover, the fumes produced by many bases are harmful to
humans/animals and are highly
= corrosive and/or explosive potentially, transportation and storage
requirements for liquid bases are
restrictive and taxing in such that you must typically haul the products in
tankers or intermediate bulk
containers (IBC) that are rated to handle such corrosive-regulated products,
creating exposure dangers for
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CA 3023705 2018-11-09

personnel having to handle them. Sodium hydroxide and its solutions, mists,
and aerosols are rapidly
damaging when they come in contact with the eyes, skin, and upper respiratory
tract causing irritation,
burns, coughing, chest pain and dyspnea. Swelling of the throat and
accumulation of fluid in the lungs
(shortness of breath, cyanosis, and expectoration) may occur. Ingestion of
sodium hydroxide can cause
severe corrosive injury to the lips, mouth, throat, esophagus, and stomach.
There is no antidote to be
administered to counteract the effects of sodium hydroxide. Treatment consists
of supportive measures.
Price fluctuations with typical commodity caustics based on industrial output
causing end users an
inability to establish long term costs in their respective budgets; severe
reaction with dermal/eye tissue;
major PPE requirements (personal protective equipment) for handling, such as
on site shower units;
extremely high corrosion rates, the need for constant expensive heating of
liquid solutions and the
aggressive non-linear raising of pH are some of the negatives to the industry
standard bases utilized, such
as sodium hydroxide.
When used to control the pH levels on surface of water/fluid systems, caustics
are exposed to
humans and mechanical devices as well as expensive pumping equipment causing
increased risk for the
operator and corrosion effects that damage equipment and create hazardous
hydrogen gas when they come
into contact with water or aluminum. When mixed with acidic or lower pH
fluids, caustics will create a
large amount of thermal energy (exothermic reaction) causing potential safety
concerns and equipment
damage, caustics typically need to be blended with fresh water to the desired
concentration requiring
companies to sometimes pre-blend off-site as opposed to blending on-site,
greatly thereby increasing costs
associated with transportation.
Typical caustics used in a pH control situation can or will cause degradation
of certain
polymers/additives/systems/formations requiring further chemicals to be added
to counter these potentially
negative effects, many offshore areas of operations have very strict
regulatory rules regarding the
transportation/handling and deployment of caustics causing greatly increased
liability and costs for the
operator.
Caustics perform many actions in the oil & gas industry and are considered
necessary to achieve
the desired production of various petroleum wells, maintain their respective
systems and aid in certain
functions (i.e. suppressing calcium & magnesium in hard waters). The
associated dangers that come with
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CA 3023705 2018-11-09

using caustics are expansive and tasking to mitigate through controls whether
they are chemically or
mechanically engineered.
Eliminating or even simply reducing the negative effects of caustics while
maintaining their
performance level is a struggle for the industry. As the public demand for the
use of cleaner/safer/greener
products increases, companies are looking for alternatives that perform the
required function without all or
most of the drawbacks associated with the use of caustics.
US patent no. 7,073,519 discloses a facility parts cleaning composition for
the processing of
(meth)acrylic acid and/or (meth)acrylic esters comprising an alkali metal
hydroxide solution, a water-
soluble amino acid, N,N'-methylene bisacrylamidc, and azobisisobutyronitrile,
and a cleaning method using
the cleaning solution composition. Disclosed are compositions including 5 to
50 wt % of at least one alkali
metal hydroxide selected from the group consisting of sodium hydroxide and
potassium hydroxide, 0.01 to
1 wt % of a water-soluble amino acid, 0.001 to 0.05 wt % of N,N'-methylene
bisacrylamide, and 0.001 to
0.05 wt % of azobisisobutyronitrile.
US patent no. 7,902,137 discloses alkaline concentrated detergent composition
for use in cleaning
hard surfaces, medical instruments and other metal components (parts, tools,
utensils, vessels, equipment).
The description states that an important aspect of the invention is the
utilization of a synergistic system of
chelants and scale inhibition components that are biodegradable. Chelation and
scale inhibition are said to
have a positive impact on cleaning performance of the compositions.
US Statutory Invention Registration no. H468 entitled "Alkaline hard-surface
cleaners containing
alkyl glycosides" discloses a cleaning composition comprising: (a) about 0.1
to 50 weight percent alkali
metal hydroxide or ammonium hydroxide; (b) about 0.1 to 40 weight percent
alkyl glycoside; and (c) about
to 95 weight percent water.
US Patent no. 9,399,589 B2 teaches the use of glycine in the making of a
synthetic base that is said
to obviate all the drawbacks of strong bases such as sodium hydroxide. It is
stated that the compound is
made by dissolving glycine in water and adding calcium hydroxide at a molar
ratio of about 1:1. Sodium
percarbonate is then dissolved in the solution to produce the new compound.
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CA 3023705 2018-11-09

US patent no. 6,387,864 discloses a laundry detergent composition comprising
about 1 to about 75
parts by weight of at least one caustic compound, about 0.5 to about 50 parts
by weight of at least one
nonionic surfactant, about 1 to about 35 parts by weight of at least one
primary amine compound.
US patent no. 5,804,541 discloses a floor stripper composition is provided,
having a pH-value
above 9.0, and comprising a soap, water and a glycine-N,N-diacetic acid
compound, which is preferably
methylglycine diacetic acid (MGDA). The diacetic acid is desirably in the form
of a divalent metal complex
thereof. The description states that a good floor stripper performance could
be obtained with this
composition owing to its low foaming behaviour.
Since several operations in the oil industry expose fluids and equipment to
very high temperatures
(some upward of 200 C), the caustic compositions used in these various
operations need to withstand these
high temperatures without losing their effectiveness. These compositions must
be capable of being used in
operations over a wide range of temperatures (even at very low temperatures
below zero) while not affecting
the equipment or people it comes in contact with.
Consequently, there is still a need for compositions for use in the oil
industry which can be used
over a range of applications which can decrease a number cf the associated
dangers/issues typically
associated with caustic applications to the extent that these caustic
compositions are considered much safer
for handling on worksites. The present invention seeks to overcome some of
drawbacks of the prior art
caustic compositions and methods using such caustic compositions.
SUMMARY OF THE INVENTION
According to a first aspect of the present invention, there is provided a
caustic composition
comprising:
- a caustic component;
- an additive adapted to provide an extended (more methodical and
linear) buffering effect to the
caustic composition as well as greatly lowering the freeze point and providing
an increased
level of dermal protection; and
- water.
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CA 3023705 2018-11-09

Preferably, the caustic component is selected from the group consisting of:
potassium hydroxide;
sodium hydroxide; lithium hydroxide; cesium hydroxide; rubidium hydroxide and
combinations thereof.
More preferably, the caustic component is selected from the group consisting
of: potassium hydroxide;
sodium hydroxide and combinations thereof. Preferably, the caustic component
is present in a
concentration of up to 40 wt% of the composition. More preferably, the caustic
component is present in a
concentration ranging from 5 to 40 wt% of the composition. Yet more
preferably, the caustic component
is present in a concentration ranging from 10 to 30 wt% of the composition.
Yet even more preferably, the
caustic component is present in a concentration ranging from 15 to 25 wt% of
the composition. According
to a preferred embodiment of the present invention, the caustic component is
present in a concentration of
approximately 25 wt% of the composition.
Preferably, the additive is selected from the group of amino acids consisting
of: alanine; argininc;
asparagine; aspartic acid; cysteine; glutamic acid; glutamine; histidine;
isoleucine; leucine; lysine;
methionine; phenylalanine; proline; serine; threonine; tryptophan; tyrosine;
valine and salts thereof.
More preferably, the additive is selected from the group consisting of: Lysine
monohydrochloride;
threonine; and methionine. Preferably also, the additive is monosodium
glutamate. Preferably, the additive
is present in a concentration ranging from 2 wt% to 25 wt% of the composition.
More preferably, the
additive is present in a concentration ranging from 4 wt% to 15 wt% of the
composition. Yet even more
preferably, the additive is present in a concentration ranging from 4 wt% to
10 wt% of the composition.
According to another aspect of the present invention, there is provided a
method of fracking a
hydrocarbon-bearing formation using a crosslinked polymer gel, said method
comprising the steps of:
- providing a hydrocarbon-bearing formation;
- providing a polymer;
- providing a cross-linking activator and adding such to the polymer;
- adding to the polymer mixture a caustic composition comprising:
- a caustic component;
- an additive adapted to provide an extended, more linear buffering effect to
the caustic
composition when such is exposed to the fluid system; and
- water;
- adding a proppant to the resulting polymer mixture; and
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CA 3023705 2018-11-09

- injecting said resulting polymer-proppant composition into the formation.
Preferably, the crosslinking component is a borate ion or a zirconate ion.
Preferably, the polymer
is a guar gum, Carboxymethyl guar gum, Hydroxymethyl guar gum;
Hydroxypropylethyl guar gum; 0-
carboxymethyl- 0-hydroxypropyl guar gum (CMHPG); Ammonium hydroxyl propyl
trimethyl chloride of
guar gum; 0-carboyxymethy1-0-2 hydroxy-3-(trimethylammonia propyl) guar gum
(CMHTPG);
Acryloyloxy guar gum; Methacryloyl guar gum; Guar gum esters such as Hydroxy
Propyl Guar (HPG),
Carboxy Methyl Guar (CMG), Carboxy Methyl Hydroxy Propyl Guar (CMHPG), and
Guar.
According to another aspect of the present invention, there is provided a
method of removing
impurities present in petroleum during the refining thereof, said method
comprising the steps of:
- providing a petroleum product to be refined;
- providing a caustic composition comprising:
- a caustic component;
- an additive adapted to provide an extended, more linear buffering effect
to the caustic
composition when such is exposed to acid; and
- water;
- adding said caustic composition to said petroleum product to be refined;
and
- allowing said caustic composition and said petroleum product to be
refined to remain in contact
with one another for a period of time determine to be sufficient for the
sufficient removal of at least one of
carbon dioxide and sulfur-containing compounds.
According to another aspect of the present invention, there is provided a use
of the composition
according to a preferred embodiment of the present invention, for the control
the pH of water based drilling
fluids.
According to another aspect of the present invention, there is provided a use
of the composition
according to a preferred embodiment of the present invention, for the breaking
down of organic matter
present in petroleum during the refining thereof.
According to another aspect of the present invention, there is provided a use
of the composition
according to a preferred embodiment of the present invention, for the removal
of various impurities during
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CA 3023705 2018-11-09

the refining stage of petroleum production. Preferably, the impurities are
selected from the group consisting
of: include: carbon dioxide and sulfur-containing compounds.
According to another aspect of the present invention, there is provided an
aqueous caustic
composition comprising:
- a caustic component;
- an amino acid additive adapted to provide an extended buffering effect to
the caustic
composition when such is exposed to an acid; and
- water;
wherein the amino acid additive is selected from the group consisting of:
alanine; arginine; asparagine;
aspartic acid; cysteine; glutamic acid; glutamine; histidine; isoleucine;
leucine; lysine; methionine;
phenylalanine; proline; serine; threonine; tryptophan; tyrosine; valine and
salts thereof, and wherein the
caustic component is present in a concentration of up to 40 wt % of the
composition and the caustic
component and the additive are present in a molar ratio ranging from 15:1 to
5:1. Preferably, the caustic
component and the additive are present in a molar ratio ranging from 12:1 to
8:1. Preferably also, the
caustic component comprises an hydroxide anion and a monovalent cation.
Preferably, the monovalent
cation is selected from the group consisting of: potassium, sodium, lithium,
cesium and rubidium. More
preferably, the cation is selected from the group consisting of: potassium and
sodium.
According to another aspect of the present invention, there is provided a use
of a buffered caustic
solution in water treatment, wherein said buffered caustic solution
comprising:
o a caustic component;
o an amino acid additive adapted to provide an extended buffering effect to
the caustic
composition when such is exposed to an acid; and
o water;
wherein the amino acid additive is selected from the group consisting of:
alanine; arginine;
asparagine; aspartic acid; cysteine; glutamic acid; glutamine; histidine;
isoleucine; leucine; lysine;
methionine; phenylalanine; proline; serine; threonine; tryptophan; tyrosine;
valine and salts thereof,
wherein the caustic component is present in a concentration of up to 40 wt %
of the composition
and the caustic component and the additive are present in a molar ratio
ranging from 15:1 to 5:1.
According to another aspect of the present invention, there is provided a
method to treat water,
wherein said method comprises the steps of:
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CA 3023705 2018-11-09

= - providing an aqueous caustic composition comprising:
o a caustic component;
o an amino acid additive adapted to provide an extended buffering effect to
the caustic
composition when such is exposed to an acid; and
o water;
wherein the amino acid additive is selected from the group consisting of:
alanine; arginine;
asparagine; aspartic acid; cysteine; glutamic acid; glutamine; histidine;
isoleucine; leucine; lysine;
methionine; phenylalanine; proline; serine; threonine; tryptophan; tyrosine;
valine and salts thereof,
wherein the caustic component is present in a concentration of up to 40 wt %
of the composition
and wherein he caustic component and the additive are present in a molar ratio
ranging from 15:1
to 5:1; and
- exposing a water requiring treatment to a pre-determined amount of
said caustic composition
for a period of time sufficient to effect the treatment intended.
BRIEF DESCRIPTION OF THE FIGURES
The invention may be more completely understood in consideration of the
following description of
various embodiments of the invention in connection with the accompanying
figures, in which:
Figure 1 depicts a titration curve of a composition of NaOH (25 wt%);
Figure 2 depicts a titration curve of a composition according to a preferred
embodiment of the
present invention, said composition comprising NaOH (25 wt%) with 5 wt% lysine
monohydrochloride;
Figure 3 depicts a titration curve of a composition according to a preferred
embodiment of the
present invention, said composition comprising NaOH (25 wt%) and 5 wt%
methionine;
Figure 4 depicts a titration curve of a composition according to a preferred
embodiment of the
present invention, said composition comprising NaOH (25 wt%) and 5 wt%
tryptophan;
Figure 5 depicts a titration curve of a composition according to a preferred
embodiment of the
present invention, said composition comprising NaOH (25 wt%) and 5 wt%
glutamic acid;
CA 3023705 2018-11-09

Figure 6 depicts a titration curve of a composition comprising NaOH (25 wt%)
and 5 wt%
threonine;
Figure 7 depicts a titration curve of a composition according to a preferred
embodiment of the
present invention, said composition comprising NaOH (25 wt%) and 5 wt% lysine;
Figure 8 depicts a titration curve of a composition according to a preferred
embodiment of the
present invention, said composition comprising NaOH (25 wt%) and 5 wt% lysine
monohydrochloride;
Figure 9 depicts a titration curve of a composition according to a preferred
embodiment of the
present invention, said composition comprising NaOH (25 wt%) and 5 wt% lysine
monohydrochloride;
Figure 10 depicts a titration curve of a composition according to a preferred
embodiment of the
present invention, said composition comprising NaOH (25wt%) and 5 wt% lysine
monohydrochloride USP;
and
Figure 11 depicts a titration curve of a composition according to a preferred
embodiment of the
present invention, said composition comprising NaOH (25 wt%) and 5 wt%
monosodium glutamate.
DESCRIPTION OF A PREFERED EMBODIMENT OF THE PRESENT INVENTION
Borate crosslinked gel fracturing fluids utilize borate ions to crosslink the
hydrated polymers and
provide increased viscosity. The polymers most often used in these fluids are
guar and HPG. The crosslink
obtained by using borate is reversible and is triggered by altering the pH of
the fluid system (increasing the
pH generates the crosslink function, decreasing the pH eliminates the
crosslink). The reversible
characteristic of the crosslink in borate fluids helps them clean up more
effectively, resulting in good
regained permeability and conductivity. The present invention can be utilized
in this type of situation all
the while having a minimal negative effect on polymer chains. The latter is
yet another advantage of a
preferred embodiment of the present invention. Borate crosslinked fluids have
proved to be highly effective
in both low and high permeability formations.
11
CA 3023705 2018-11-09

To achieve an optimal crosslinking of borate crosslinked guar gel, a pH
between 8.5 and 9.0 is
necessary. This is a very narrow pH window. A common drawback of using neat
caustic is that, as a strong
base, a pH in that range can be quite difficult to adjust. A slight difference
in dosage can result in a high pH
shift, this results in the breakdown of the crosslinking in the gel.
In an attempt to overcome the drawback of using strong caustic agents in the
presence of
crosslinked gels, or at least to compensate and create a buffer which allows
some flexibility in the dosage,
a crosslinker and guar gum is added on location on the fly with special
equipment.
According to a preferred embodiment of the present invention, it is desirable
to have a buffered
caustic solution, which enables one to adjust the pH more precisely in a
desired range (in other words it is
more forgivable in terms of overdosage). Such a buffer provides a substantial
advantage over the use of a
neat caustic composition.
According to another preferred embodiment of the present invention, it is
desirable to have a
buffered caustic solution in water treatment. Caustics such as sodium
hydroxide can be used to raise the
pH of water supplies. Increased pH renders the water less susceptible to
corrode pipes and reduces the
amount of free metals including copper and other metals which can be found in
drinking water.
According to a preferred embodiment of the present invention, there is
provided a method to treat
water, wherein said method comprises the steps of:
- providing an aqueous caustic composition comprising:
o a caustic component;
o an amino acid additive adapted to provide an extended buffering effect to
the caustic
composition when such is exposed to an acid; and
o water;
wherein the amino acid additive is selected from the group consisting of:
alanine;
arginine; asparagine; aspartic acid; cysteine; glutamic acid; glutamine;
histidine;
isoleucine; leucine; lysine; methionine; phenylalanine; proline; serine;
threonine;
= tryptophan; tyrosine; valine and salts thereof, and wherein the caustic
component
is present in a concentration of up to 40 wt % of the composition and the
caustic
12
CA 3023705 2018-11-09

component and the amino acid additive are present in a molar ratio ranging
from
15:1 to 5:1; and
- exposing a water requiring treatment to a pre-determined amount of
said caustic composition
for a period of time sufficient to effect the treatment intended.
Example 1
Preparation of a caustic composition according to a preferred embodiment
A composition according to a preferred embodiment of the present invention was
prepared by
providing 100m1 of 25 wt% NaOH solution. The NaOH solution is then mixed with
the appropriate weight
of additive, in this case, lysine to be present in an amount of 5 wt%, to
obtain the desired weight %
concentration. The resulting composition is mixed until one visually
determines that solubilization is
completed.
Titration of the composition
The titration of the composition of Example 1 was performed in order to assess
its buffering ability.
In order to do so, 1 ml of the buffer (composition of Example 1) was drawn and
placed in a flask, the buffer
was then diluted in 100 ml of distilled water. The resulting solution was
titrated with 1 N HCI standard.
The pH was continuously recorded with a pH meter. The solution was gently
stirred with a magnetic stir
bar during the measurements. Prior to recording the pH after each addition of
HCl, sufficient time was
given to allow for the pH to stabilize. The resulting titration curve
associated with Example 1 is found in
Figure 7.
As can be seen by referring to Figures 1 to 11, preferred embodiments of the
present invention (set
out in Figures 2 to 11) displayed an extended / linear buffering effect when
exposed to acid addition as
compared to caustic composition free of additive. This advantageous buffering
effect translates into an
increased ability to control the pH of crosslinked gels during fracking
operations. This is even more
advantageous when the pH adjustment is done on the fly. Preferred compositions
of the present invention
display a strong caustic character, extended linear buffering effect (compared
to neat caustic), greatly
reduced freeze point and minimized dermal damage upon direct contact with
human skin.
According to a preferred embodiment of the present invention, certain
additives such as lysine
monohydrochloride, and threonine can buffer the pH drop of a 25 wt% caustic
solution in the pH range of
13
CA 3023705 2018-11-09

8.25 to 10. Such a buffering effect is desirable in fracking operations to
maintain the integrity of a guar gel
based polymeric system.
According to a preferred embodiment of the present invention, a caustic
composition comprising
lysine-HCl as additive can have a freezing point as low as -45 C. This is a
substantial decrease in the freeze
point compared to -18 C for 25 wt% NaOH. This proves to be highly desirable
for winter operations in the
oil and gas industry.
Dermal Test
Human dermal tests were performed to assess the safety of inadvertent exposure
to a composition
according to a preferred embodiment of the present invention.
The tests have determined that human skin having an extended exposure time
between 20 to 30
minutes showed minimal signs of damage (i.e. skin irritation) from direct
exposure of the composition. This
stands in stark contrast with pure NaOH (25%) which, when dropped on the skin
causes immediate burning
of the skin, followed with scarring.
According to a preferred embodiment, it is desirable to use REACH-Ed-IA
approved products such
as lysine and methionine. To have REACH-ECHA approved components provides more
opportunities to
apply the present technology all the while improving recovery and minimizing
environmental damage.
According to another application of the composition according to the preferred
embodiment of the
present invention, a hot solution of the caustic composition according to a
preferred embodiment of the
present invention can be used to dissolve aluminium-containing minerals in the
bauxite. This, as a result,
forms a supersaturated solution of sodium aluminate. When the solution is
cooled it will yield a solid form
of sodium aluminate. This sodium aluminate can be employed in water treatment,
in construction to
accelerate the solidification of concrete, in the paper industry, to make fire
bricks production, to
manufacture alumina.
According to another preferred embodiment of the present invention, it is
desirable to have a
buffered caustic solution in water treatment. Caustics such as sodium
hydroxide can be used to raise the
14
CA 3023705 2018-11-09

pH of water supplies. Increased pH renders the water less susceptible to
corrode pipes and reduces the
amount of free metals including copper and other metals which can be found in
drinking water.
Although a few embodiments have been shown and described, it will be
appreciated to those skilled
in the art that various changes and modifications can be made to the
embodiments described herein. The
terms and expressions used in the above description have been used herein as
terms of description and not
of limitation, and there is no intention in the use of such terms and
expressions of excluding equivalents of
the features shown and described or portions thereof, it being recognized that
the invention is defined and
limited only by the claims that follow.
CA 3023705 2018-11-09

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Administrative Status

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Event History

Description Date
Inactive: Multiple transfers 2023-12-14
Inactive: Grant downloaded 2023-10-26
Inactive: Grant downloaded 2023-10-26
Letter Sent 2023-08-29
Grant by Issuance 2023-08-29
Inactive: Cover page published 2023-08-28
Pre-grant 2023-06-29
Inactive: Final fee received 2023-06-29
Notice of Allowance is Issued 2023-05-01
Letter Sent 2023-05-01
Inactive: Recording certificate (Transfer) 2023-04-21
Inactive: Q2 passed 2023-04-17
Inactive: Approved for allowance (AFA) 2023-04-17
Inactive: Multiple transfers 2023-03-28
Change of Address or Method of Correspondence Request Received 2023-02-15
Amendment Received - Response to Examiner's Requisition 2023-02-15
Amendment Received - Voluntary Amendment 2023-02-15
Examiner's Report 2022-11-08
Inactive: Report - No QC 2022-08-04
Letter Sent 2021-05-26
Change of Address or Method of Correspondence Request Received 2021-05-12
Request for Examination Requirements Determined Compliant 2021-05-12
All Requirements for Examination Determined Compliant 2021-05-12
Request for Examination Received 2021-05-12
Common Representative Appointed 2020-11-07
Application Published (Open to Public Inspection) 2020-05-09
Inactive: Cover page published 2020-05-08
Common Representative Appointed 2019-10-30
Common Representative Appointed 2019-10-30
Inactive: IPC assigned 2019-02-19
Inactive: IPC assigned 2019-01-11
Inactive: IPC assigned 2019-01-07
Inactive: First IPC assigned 2019-01-07
Inactive: IPC assigned 2019-01-07
Inactive: IPC assigned 2019-01-07
Inactive: IPC assigned 2019-01-07
Filing Requirements Determined Compliant 2018-11-20
Inactive: Filing certificate - No RFE (bilingual) 2018-11-20
Inactive: Office letter 2018-11-19
Application Received - Regular National 2018-11-14

Abandonment History

There is no abandonment history.

Maintenance Fee

The last payment was received on 2022-10-28

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  • the reinstatement fee;
  • the late payment fee; or
  • additional fee to reverse deemed expiry.

Please refer to the CIPO Patent Fees web page to see all current fee amounts.

Fee History

Fee Type Anniversary Year Due Date Paid Date
Application fee - standard 2018-11-09
MF (application, 2nd anniv.) - standard 02 2020-11-09 2020-09-14
Request for examination - standard 2023-11-09 2021-05-12
MF (application, 3rd anniv.) - standard 03 2021-11-09 2021-11-05
MF (application, 4th anniv.) - standard 04 2022-11-09 2022-10-28
Registration of a document 2023-03-28
Final fee - standard 2023-06-29
MF (patent, 5th anniv.) - standard 2023-11-09 2023-11-01
Registration of a document 2023-12-14
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
DORF KETAL CHEMICALS FZE
Past Owners on Record
CLAY PURDY
MARKUS WEISSENBERGER
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Cover Page 2023-08-14 1 27
Description 2018-11-09 15 660
Abstract 2018-11-09 1 9
Claims 2018-11-09 5 166
Drawings 2018-11-09 6 82
Cover Page 2020-04-03 1 25
Claims 2023-02-15 3 165
Filing Certificate 2018-11-20 1 205
Courtesy - Acknowledgement of Request for Examination 2021-05-26 1 436
Commissioner's Notice - Application Found Allowable 2023-05-01 1 579
Final fee 2023-06-29 5 135
Electronic Grant Certificate 2023-08-29 1 2,527
Courtesy - Office Letter 2018-11-19 1 47
Change to the Method of Correspondence 2021-05-12 5 164
Request for examination 2021-05-12 5 164
Examiner requisition 2022-11-08 5 225
Amendment / response to report 2023-02-15 10 433
Change to the Method of Correspondence 2023-02-15 3 54