[0001] The present invention relates to the use of water based functional fluids which can
be used for example as hydraulic fluids, lubricants, drilling or cutting fluids.
[0002] Functional fluids based upon mixtures of water and polyether glycols are well known
and are used in a wide variety of applications eg as cutting fluids, hydraulic fluids
and the like.
[0003] Typical formulations of water-based hydraulic fluids (known as HF-C fluids) comprise
approximately 15-30% of a high-viscosity polyether glycol, and 35-45% water, with
the balance (up to 50%) being simple glycol and small amounts of additives known to
the skilled man. Typically these hydraulic fluids have a viscosity of 32-68 cSt at
40°C.
[0004] There is a growing trend however to reduce the polyether glycol content of such functional
fluids. For example it would ultimately be desirable to reduce the polyether glycol
content of hydraulic fluids to 10% or possibly even less. There is also a trend to
produce what can be described as High Water Based Fluids (HWBFs), containing typically
50-98 percent water, by additionally removing some or all of the glycol.
[0005] A problem arises when attempts are made to reduce the polyether glycol content of
hydraulic fluids in that the viscosity of the hydraulic fluid is reduced. This arises
because standard polyether glycol fluids do not possess sufficient thickening power.
Simply increasing the viscosity of the polymer does not achieve the required effect,
because the increase in solution viscosity becomes marginal, and the polymer becomes
unstable under conditions of high shear.
[0006] It has previously been proposed for example in US 4 767 555 and US 4 288 639 to achieve
the required viscosity of such hydraulic fluids by incorporation of small amounts
of materials which (a) are water compatible and (b) increase the viscosity of the
hydraulic fluids by intermolecular association in solution. Such materials are known
as associative thickeners.
[0007] The hydraulic fluids previously described as high-water-based fluids (HWBFs), usually
incorporating either no simple glycol, or only small amounts as antifreeze, have a
number of disadvantages when compared to HFC water glycol fluids, viz
i) Although the HWBFs normally exhibit 'permanent shear stability', that is the viscosity
of the fluid remains stable over a long period of operation, they none-the-less exhibit
temporary loss oF viscosity in high shear zones, as evidenced by loss of flow rate
and pump efficiency in hydraulic systems, in other words they lack 'temporary shear
stability'.
ii) Under such conditions of temporary viscosity loss, hydrodynamic lubricity of the
fluid also suffers. Lubrication is maintained only by additives which provide boundary
lubrication (EP additives). Despite such additives being highly developed, these conditions
can result in enhanced wear. Additionally the best of these additives in many instances
are toxic, hydrolytically unstable and environmentally undesirable.
iii) The viscosity index of such fluids is often poor which can give problems with
pump start-up.
iv) HWBF's are sensitive to water loss, which has a dramatic and undesirable effect
on fluid viscosity.
[0008] US 3538033 discloses a family of polyether derivatives of diepoxides which can be
used as thickeners in textile printing emulsions, cosmetic emulsions, aqueous pigment
suspensions and the like.
[0009] The problem to be solved is therefore to produce functional fluids, suitable for
the applications described above, which have good permanent and temporary shear stability,
contain low concentrations of the associative thickeners, have good resistance to
water loss in terms of viscosity change, have good apparent viscosity indices, and
which maintain hydrodynamic lubrication under high shear conditions.
[0010] According to the present invention there is provided a functional fluid composition
for use as a hydraulic fluid, lubricant, a cutting fluid or a drilling fluid which
comprises
(a) from 20 to 98% by weight water
(b) from 0 to 80% by weight of a glycol and
(c) from 0.5 to 25% by weight of a thickening agent prepared by (a) relatively reacting
one mole of a monofunctional, active-hydrogen- containing compound having at least
10 carbon atoms with between 20 and 400 moles of one or more alkylene oxides and (b)
thereafter reacting the product of step (a) with a diepoxide in an amount such that
the molar ratio of diepoxide to hydroxyl groups in the product of step (a) is between
0.2:1 and 5:1.
[0011] The present invention solves the problem defined above by employing a thickening
agent of the type defined in US 3538033 in the applications described above, together
with the formulation technology which is detailed below.
[0012] Considering the water component of the composition first, it is preferred that this
comprises between 36 and 95% of the functional fluid most preferably between 45 and
80%.
[0013] As regards the glycol, this can be in principle any glycol which is miscible with
water and includes monoethylene glycol and monopropylene glycol and low molecular
weight oligomers thereof (ie having up to 6 ethylene and/or propylene glycol units).
Preferably the glycol is selected from monoethylene glycol, diethylene glycol and
triethylene glycol. It is preferred that the glycol comprises between 20 and 60% of
the functional fluid.
[0014] The first stage of preparing the thickening agent involves reacting the monofunctional
active hydrogen containing compound with one or more alkylene oxides. By the term
'active-hydrogen- containing compound' is meant one which contains hydrogen measurable
by the Zerewitinoff active hydrogen test. Such compounds include alcohols, phenols,
thiols, fatty acids and amines. The preferred compounds are C₁₆ to C₂₀ monohydric
alcohol or thiols, C₁₆ to C₂₀ alkyl phenols and C₁₆ to C₂₀ aliphatic amines.
[0015] The active hydrogen containing compound is alkoxylated with one or more alkylene
oxides using either a base or a Lewis acid as a catalyst. Typically the alkylene oxide
is one or more of ethylene oxide, propylene oxide or the isomers of butylene oxide.
Suitably between 20 and 400 moles of the alkylene oxide are added to the active hydrogen
containing compound of which 20 to 100 mole % (most preferably 65 to 85 mole %) is
ethylene oxide and 0 to 80% (most preferably 15 to 35%) is propylene and/or butylene
oxide.
[0016] In the second stage of manufacture the product of the first stage is reacted with
a diepoxide. The diepoxide can in principle by any organic compound having two epoxide
groupings. Suitable diepoxides are those having between 4 and 30 carbon atoms and
include vinylcyclohexene diepoxide, bisphenol A/epichlorohydrin condensate and the
like. It is preferred to use the diepoxide in amounts such that the molar ratio of
epoxide groups to hydroxyl groups (in the product of stage 1) is in the range 0.2
to 1 to 5 to 1. The second stage of the process can also be catalysed by either a
base or a Lewis acid.
[0017] It is preferred that the thickening agent comprises between 2 and 10% by weight of
the functional fluid composition. It is also preferred that the thickener itself should
have a neat viscosity in excess of 4000 cSt at 40°C.
[0018] Concerning the antiwear components, these are typically metal or amine salts of organo
sulphur, phosphorus or boron derivatives, or carboxylic acids. Typically these include
salts of C₁ to C₂₂ carboxylic acids, aliphatic or aromatic; sulphur acids such as
aromatic sulphonic acids, phosphorus acids, for example acid phosphate esters and
analogous sulphur compounds, eg thiophosphoric and dithiophosphoric acid. Many further
antiwear agents are suitable, and known to the skilled man.
[0019] Inhibitors for corrosion of metals can be organic or inorganic, for example metal
nitrites, hydroxyamines, neutralised fatty acid carboxylates, phosphates, sarcosines
and succinimides etc. Most useful are amines such as alkanolamines, e.g. ethanolamine,
diethanolamine and triethanolamine. Non-ferrous metal inhibitors include for example
aromatic triazoles.
[0020] It is preferred to include in the formulation 0.5 to 15% of a surfactant as a co-thickening
agent, which may be non-ionic, cationic, anionic or amphoteric. Examples of suitable
surfactants include linear alcohol alkoxylates, nonylphenol ethoxylates. fatty acid
soaps, amine oxides etc. Most preferred are linear secondary alcohol alkoxylates,
eg those commercially available from BP Chemicals under the registered trade mark
Softanol. The surfactants behave synergistically with the associative thickener, such
that a given viscosity can be achieved with a lower total thickener content of the
blend compared to use of the associative thickener alone.
[0021] In addition to the above the functional fluid composition may also contain optional
components such as extreme pressure additives, antifoams, antimicrobials and the like
which are well known to the skilled man. It is also possible to add further known
thickening agents and co-thickening agents if desired.
[0022] The functional fluid compositions of the present invention may be prepared by mixing
the four main components and any additional materials which are required in a vessel
of suitable size.
[0023] In the preferred embodiments of the invention, that is those formulations containing
20 or more percent of glycol, it has been found that temporary shear stability is
conferred to the fluids. This enhances the capability of the fluids to provide hydrodynamic
lubrication under high shearing conditions. The presence of the 20 or more percent
glycol, and of the surfactant cothickener also improves the apparent viscosity index
of the fluids when compared against fluids containing no glycol or surfactant.
[0024] In those embodiments of the invention containing less than 20 percent glycol, the
problem of temporary shear is also addressed, by use of associative thickeners of
the present invention with high inherent polymer viscosity (eg greater than 20,000
cSt at 40°C). In high shear environments, thickening achieved by association is lost
when the fluids shear temporarily. However, the viscosity of the fluid is maintained
at an intermediate level by the normal thickening of a high viscosity polymer, typically
to a level of 10-20 cSt at 50°C. This limits the loss of pump efficiency, and ensures
that hydrodynamic lubricity is retained. This approach also enhances the characteristics
of the fluid concerning viscosity change on water loss and viscosity index.
[0025] The functional fluid compositions of the present invention are particularily useful
as hydraulic fluids in piston, gear or vane hydraulic pumps, motors and general hydraulic
systems, eg hydraulic rams, robots and the like.
[0026] The invention is now illustrated by the following examples:
Example 1
[0027] A commercial sample of oleyl/cetyl alcohol (85/15) was catalysed with potassium hydroxide
(0.3% by weight on the target alkoxylate), dried, and reacted with a 70/30 (weight/weight)
mixture of ethylene oxide and propylene oxide at 115-125°C to produce an alkoxylate
having an experimentally determined molecular weight of 6000 (by hydroxyl determination).
[0028] 500 grams of the above un-neutralised alkoxylate was reacted at 130°C with 15.9 grams
bisphenol A/epichlorohydrin condensate (Epikote 828 - ex Shell) for three hours. The
residual catalyst was removed by treatment with magnesium silicate to leave an associative
thickener with a neat viscosity of 5000 cSt @ 40°C. A 10% aqueous solution viscosity
was determined as 193 cSt @ 40°C.
Example 2
[0029] 500 grams of the above-mentioned un-neutralised alkoxylate from example 1 was reacted
at 130°C with 31.8 grams of bisphenol A/epichlorohydrin condensate for 3 hours, the
catalyst was removed with magnesium silicate treatment, to leave an associative thickener
with a neat viscosity of 17,300 cSt @ 40°C. A 10% aqueous solution viscosity was determined
as 2100 cSt @ 40°C.
Example 3
[0031] A commercial sample of oleyl/cetyl alcohol (85/15) was reacted in the manner described
in example 1 with an 80/20 mixture of ethylene oxide and propylene oxide to produce
an alkoxylate having a molecular weight of 6000.
[0032] 300 grams of the above-mentioned un-neutralised polyalkylene glycol was reacted with
14.0 grams of vinylcyclohexene diepoxide for three hours at 140-150°C. The resulting
associative thickener had a neat viscosity of 4,900 cSt @ 40°C and a 10% aqueous solution
viscosity of 1427 cSt @ 40°C.
Example 4
[0033] A commercial sample of oleyl/cetyl alcohol (85/15) was reacted in the manner described
in example 1 with an 75/25 mixture of ethylene oxide and propylene oxide to produce
an intermediate having a molecular weight of 2950, then with further ethylene oxide
to produce an alkoxylate having a molecular weight of 3100.
[0034] 2000 grams of the above mentioned un-neutralised polyalkylene glycol was reacted
with 175 grams of vinylcyclohexene diepoxide at 140-150°C for 6 hours to yield an
associative thickener with a 10% aqueous solution viscosity of 1742 cSt.
Examples 5 - 8
[0035] Dodecan-1-ol, Tetradecan-1-ol, Hexadeca-1-ol and Octadecan-1-ol were reacted under
base catalysis with 80/20 blends of ethylene oxide/propylene oxide to produce alkoxylates
having molecular weights of 6000. 200 grams of each alkoxylate was reacted with 9.4
grams of vinylcyclohexane diepoxide in the manner described for example 3 to yield
four associative thickeners. The products were used to provide a comparison of solution
viscosity versus hydrophobe chain length.
EXAMPLE |
Comparison |
5 |
6 |
7 |
8 |
PRODUCT |
Breox 75W18000* |
C-12 |
C-14 |
C-16 |
C-18 |
Viscosity, neat, cSt @ 40°C |
18,000 |
22,400 |
10,400 |
27,400 |
21,400 |
Viscosity, 10%, cSt @ 40°C |
5 |
117 |
461 |
4,680 |
34,000 |
* standard polyglycol thickener. |
Example 9
[0036] The thickener (8%) from example 1 was formulated into a hydraulic fluid of 46 cSt
at 40°C containing water (36%), diethylene glycol (50%), a fatty acid and morpholine.
This was subjected to a four ball test (IP239) at 40 kg for 1h, and gave a wear scar
of 0.56 mm, a result similar to that of a similarly formulated hydraulic fluid using
15% of a conventional polyglycol thickener.
[0037] The same thickener at a level of 7% in a high water based fluid of 46 cSt at 40°C
was subjected to 50 passes in a Kurt Orban shear stability tester (IP294) and suffered
no permanent loss of solution viscosity.
Example 10
[0038] The thickener from example 4 was formulated at a level of 8% into a hydraulic fluid
containing 30% diethylene glycol and 58% water, the balance being an antiwear and
anticorrosion package. The said hydraulic fluid was circulated over 24 hours in a
7 kW Vickers PFB-5 axial piston pump at 50°C and 170 bar. The flow rate, which can
be directly related to the fluid viscosity, was monitored to indicate viscosity in
the high shear regions of the pump. The said hydraulic fluid was compared to a similar
hydraulic fluid containing only 10% diethylene glycol and 80% water, and with a further
hydraulic fluid, based on a commercially available, low-viscosity, associative thickener,
a fatty alcohol ethoxylate capped with an olefin epoxide, and containing no diethylene
glycol.
|
Absolute Viscosity cP @ 47°C |
Apparent Viscosity in Shear Zone cP |
% Retained Viscosity under High Shear |
Pump Flow l/m |
Example 10 |
38 |
31 |
81% |
14.6 |
10% DEG Fluid |
27 |
12 |
44% |
14.11 |
Fluid from commercial low viscosity Associative Thickener |
21 |
3.4 |
16% |
12.46 |
Example 11
[0039] The thickener from example 1 (6.2%) and a 5 mole ethoxylate of a linear secondary
C-12/14 alcohol (1.55%) (Softanol 50 - ex BP Chemicals) were blended with diethylene
glycol (40%) and water (50%), the balance consisting of functional antiwear, anticorrosion
and antifoam agents (2.25%) to give a hydraulic fluid of 45.5 cSt @ 40°C. The following
data were determined.
Four ball wear scar, mm (1h, 40kg, IP239): 0.61
Shear Stability (IP294), % viscosity change: -7
Example 12
[0040] The associative thickener from example 3 (3.6%) and a 5-mole ethoxylate of a linear
secondary C-12/14 alcohol (0.9%) were blended with diethylene glycol (20%) and water
(73.4%), the balance being additives (2%), to give a hydraulic fluid of 49.3 cSt @
40°C. The following data were determined.
Four ball wear scar, mm (1h, 40kg, IP239): 0.62
Shear Stability (IP294), % viscosity change: +5
Example 13
[0041] The associative thickener from example 3 (5.4%) and a 12 mole ethoxylate of a linear
secondary C-12/14 alcohol (3.6%) (Softanol 120 - ex BP Chemicals) were blended with
diethylene glycol (39%) and water (50%), the balance consisting of antiwear anticorrosion,
antifoam additives (2%), to give a hydraulic fluid of 46.8 cSt @ 40°C. The following
data were determined.
Four ball wear scar, mm (1h, 40kg, IP239): 0.61
Shear Stability (IP294), % viscosity change: +2.9
Example 14
[0042] The thickener from example 2 (5.0%) and a 12 mole ethoxylate of a linear, secondary,
C12/14 alcohol (1.25%) were blended with diethylene glycol (20%) and water (70%),
the balance consisting of antiwear, anticorrosion and antifoam agents (3.75%) to give
a hydraulic fluid of 46.1 cSt @ 40°C. The following data were determined.
Four ball wear scar, mm (1h, 40kg, IP239): 0.68
Example 15
[0043] To demonstrate the effect of diethylene glycol on apparent viscosity index two ISO
68 fluids were prepared from the thickener from example 3. Fluid 1 containing 6.0
percent of thickener, 30 percent of diethylene glycol and 64 percent of water. Fluid
2 containing 5.0 percent thickener and 95 percent water. The combined effect of the
presence of diethylene glycol and the slightly increased thickener requirement in
fluid 1 results in a significantly lower viscosity fluid at 20°C than that observed
for fluid 2, demonstrating that the apparent viscosity index of fluid 1 is higher
than that of fluid 2.
|
Visc. @ 40°C, cSt |
Visc. @ 20°C, cSt |
Fluid 1 |
72.5 |
585 |
Fluid 2 |
71.5 |
985 |
Example 16
[0044] To demonstrate the effect of co-thickeners on apparent viscosity index, two fluids
of 550 cSt @ 40°C were prepared as follows: Fluid 1 contained 6.0 percent of thickener
from example 2, 4.0 percent of a 12 mole ethoxylate of a C-12/14 linear secondary
alcohol, 10 percent diethylene glycol and 80 percent water. Fluid 2 contained 10.0
percent thickener from example 2, 10 percent diethylene glycol and 80 percent water.
The presence of surfactant in fluid 1 and reduced thickener requirement results in
a significantly lower viscosity fluid at 20°C than observed for fluid 2, demonstrating
that the apparent viscosity index of fluid 1 is higher than that for fluid 2.
|
Visc. @ 40°C, cSt |
Visc. @ 20°C, cSt |
Fluid 1 |
550 |
4000 |
Fluid 2 |
550 |
5500 |
1. A functional fluid composition for use as a hydraulic fluid, lubricant, cutting
fluid or drilling fluid which comprises
(a) from 20 to 98% by weight water
(b) from 0 to 80% by weight of a glycol, and
(c) from 0.5 to 25% by weight of a thickening agent prepared by (a) relatively reacting
one mole of a monofunctional active-hydrogen-containing compound having at least
10 carbon atoms with between 20 and 400 moles of one or more alkylene oxides and (b)
thereafter reacting the product of step (a) with a diepoxide in an amount such that
the molar ratio of diepoxide to hydroxyl groups in the product of step (a) is between
0.2:1 and 5:1.
2. A functional fluid composition as claimed in claim 1 further comprising functional
components for preventing wear and corrosion.
3. A functional fluid composition as claimed in claim 1 comprising from 35 to 95%
by weight water.
4. A functional fluid composition as claimed in claim 1 comprising from 20 to 60%
by weight glycol.
5. A functional fluid composition as claimed in claim 1 comprising 2 to 10% by weight
of the thickening agent
6. A functional fluid as claimed in claim 1 or claim 4 further comprising 0.5 to 15%
by weight of a non-ionic, cationic, anionic or amphoteric surfactant.
7. A functional fluid composition as claimed in claim 1 comprising 0 to 20% by weight
glycol and 0.5 to 25% by weight of a thickening agent having a neat viscosity greater
than 20,000 cSt at 40°C.
8. A process for preparing a functional fluid as defined in claim 1 which comprises
mixing the required amounts of water, glycol and thickening agent.
9. A process as claimed in claim 8 in which functional components for preventing wear
and corrosion are added during mixing.