Technical Field
[0001] The present invention relates to a lubricating oil composition for a rotary gas compressor
and a rotary gas compressor filled with the same.
Background Art
[0002] A rotary gas compressor, which generates less vibration than a reciprocating gas
compressor, is operated with a massive amount of a lubricating oil being injected,
so that a temperature of discharged gas can be lowered. Among the rotary gas compressor,
an oil-cooling screw compressor, which is a positive displacement type, has features
of a rotary type as well as features of the positive displacement type. Owing to the
features such as high efficiency, compact size and long-period continuous operation,
the oil-cooling screw compressor has been widely used in the industry (for example,
Patent Documents 1 and 2). A lubricating oil having a high kinematic viscosity of
more than 5 mm
2/s at 100 degrees C is typically used for such compressor.
Disclosure of the Invention
Problems to Be Solved by the Invention
[0004] Since such a typical rotary gas compressor (oil-cooling screw compressor) as disclosed
in Patent Documents 1 and 2 has used the lubricating oil of high viscosity as described
above, a driving power becomes excessive when the rotary gas compressor is operated.
Resultantly, a sufficient performance for energy-saving has not been obtainable.
Accordingly, an object of the invention is to provide a lubricating oil composition
for a rotary gas compressor and a rotary gas compressor filled with the same, the
lubricating oil composition having a sufficient lubricity performance as well as excellent
capability of energy-saving and reducing a lubricating oil consumption.
Means for Solving the Problems
[0005] As a result of a dedicated studies for solving the problem, the inventors have found
that a lubricating oil composition is particularly excellently applicable to a rotary
gas compressor when a kinematic viscosity, a flash point and a distillation temperature
of the lubricating oil composition are within a particular range, and then the invention
have been achieved.
[0006] The invention provides a lubricating oil composition for a rotary gas compressor
and a rotary gas compressor filled with the same as described below:
- (1) a lubricating oil composition for a rotary gas compressor having a kinematic viscosity
of 5 mm2/s or less at 100 degrees C; a flash point of 200 degrees C or more; and 5 volume
% distillation temperature of 350 degrees C or more;
- (2) the lubricating oil composition for the rotary gas compressor as described in
(1), in which a kinematic viscosity at 40 degrees C is 28 mm2/s or less;
- (3) the lubricating oil composition for the rotary gas compressor as described in
(1) or (2), in which at least either one of a phosphorous extreme pressure agent and
an antioxidant is contained;
- (4) the lubricating oil composition for the rotary gas compressor as described in
(3), in which the phosphorous extreme pressure agent is at least either one of an
orthophosphoric ester and an amine salt of a phosphate ester;
- (5) the lubricating oil composition for the rotary gas compressor as described in
(3) or (4), in which the antioxidant is at least either one of an amine compound,
a phosphorous compound, a sulfur compound and a phosphorous/sulfur containing compound;
and
- (6) A rotary compressor filled with the lubricating oil composition for the rotary
gas compressor as described in any one of (1) to (5).
[0007] When the lubricating oil composition for the rotary gas compressor according to the
above aspect of the invention is filled in the rotary gas compressor and the rotary
gas compressor is operated, a sufficient lubricity performance is maintainable, while
an energy-saving effect is excellent owing to a low kinematic viscosity. Further,
owing to a low evaporativity of the lubricating oil composition, an evaporation loss
is small even when the rotary gas compressor is operated for long hours. The lubricating
oil composition for the rotary gas compressor according to the above aspect of the
invention is considerably effective particularly when being filled in an oil-cooling
crew compressor.
Best Mode for Carrying Out the Invention
[0008] Embodiments of the invention will be described in detail below. A lubricating oil
composition for a rotary gas compressor according to an aspect of the invention (referred
to as "the composition" hereinafter) contains a lubricating base oil and an additive,
the composition having a kinematic viscosity of 5 mm
2/s or less at 100 degrees C, a flash point of 200 degrees C or more and 5 volume %
distillation temperature of 350 degrees C or more.
The lubricant base oil is not particularly limitative, but any oil typically used
as a lubricant base oil can be used irrespective of a mineral oil or a synthetic oil.
Preferably, examples of the mineral oil may include paraffinic and naphthenic base
oils which can be obtained by subjecting a lubricating oil fraction produced by atmospheric-
and vacuum-distillation of a crude oil, to any suitable combination of refining processes
selected from solvent-deasphalting, solvent-extracting, hydrocracking, solvent-dewaxing,
catalytic-dewaxing, hydrorefining, sulfuric acid treatment and clay treatment.
[0009] Preferably, examples of the synthetic oil may include: a poly-α-olefin (1-octene
oligomer, 1-decene oligomer and the like), a polybutene, an isoparaffin, an olefin
copolymer (an ethylene-propylene copolymer and the like), an alkylbenzene, an alkyl
naphthalene, monoester (butyl stearate and the like), a dibasic acid ester (ditridecyl
glutarate, di-2-ethylhexyladipate, diisodecyladipate, ditridecyladipate, di-2-ethylhexlsebacate
and the like), a tribasic acid ester (tri-merit acid ester and the like), a polyol
ester (trimethylol propane caplyrate, trimethylol propane pelargonate, pentaerythritol
2-ethylhexanoate, pentaerythritol pelargonate, and the like), a polyoxyalkylene glycol,
a dialkyl diphenyl ether, an alkyl diphenyl sulfide, a polyphenyl ether, silicone
oil (dimethyl silicone and the like) and a perfluoropolyether.
[0010] These mineral oils and synthetic oils may be singularly used, or two or more base
oils selected from these oils may be mixed at any rate in use.
The base oil of any viscosity may be used for the composition. However, in consideration
of lubricity, cooling performance and friction loss at agitation, it is desirable
to use the base oil with a kinematic viscosity of 1 to 10,000 mm
2/s at 40 degrees C, preferably 5 to 100 mm
2/s, more preferably 10 to 68 mm
2/s. The base oil for the composition may be preferably selected from API (American
Petroleum Institute) classification groups II to IV.
[0011] It is preferable that the lubricating oil composition for the rotary gas compressor
according to the aspect of the invention contains at least either one of a phosphorous
extreme pressure agent and an antioxidant.
The phosphorous extreme pressure agent is preferably orthophosphoric esters, phosphite
esters, acidic phosphate esters, acidic phosphite esters or an amine salt thereof.
The orthophosphoric ester may be exemplified by a triaryl phosphate, a trialkyl phosphate,
a trialkyl aryl phosphate, a triaryl alkyl phosphate and a trialkenyl phosphate, examples
of which may include: a triphenyl phosphate, a tricresyl phosphate, a benzyl diphenyl
phosphate, an ethyl diphenyl phosphate, a tributyl phosphate, an ethyl dibutyl phosphate,
a cresyl diphenyl phosphate, a dicresyl phenyl phosphate, an ethylphenyl diphenyl
phosphate, a diethylphenyl phenyl phosphate, a propylphenyl diphenyl phosphate, a
dipropylphenyl phenyl phosphate, a triethylphenyl phosphate, a tripropylphenyl phosphate,
a butylphenyl diphenyl phosphate, a dibutylphenyl phenyl phosphate, a tributylphenyl
phosphate, a trihexyl phosphate, a trinormal octyl phosphate, a tri(2-ethylhexyl)
phosphate, a tridecyl phosphate, a trilauryl phosphate, a trimyristyl phosphate, a
tripalmityl phosphate, a tristearyl phosphate, a trioleyl phosphate and the like.
[0012] Examples of the phosphite ester may include: a triethyl phosphite, a tributyl phosphite,
a triphenyl phosphite, a tricresyl phosphite, a tri(nonylphenyl)phosphite, a tri(2-ethylhexyl)phosphite,
a tridecyl phosphite, a trilauryl phosphite , a triisooctyl phosphite, a diphenylisodecyl
phosphite, a tristearyl phosphite, a trioleyl phosphite and the like.
Examples of the acidic phosphate ester may include: a 2-ethylhexyl acid phosphate,
a dinormal octyl acid phosphate, an ethyl acid phosphate, a butyl acid phosphate,
an oleyl acid phosphate, a tetracosyl acid phosphate, an isodecyl acid phosphate,
a lauryl acid phosphate, a tridecyl acid phosphate, a stearyl acid phosphate, an isostearyl
acid phosphate and the like.
[0013] Examples of the acidic phosphite ester may include: a diethyl hydrogen phosphite,
a dibutyl hydrogen phosphite, a dilauryl hydrogen phosphite, a dioleyl hydrogen phosphite,
a distearyl hydrogen phosphite, a diphenyl hydrogen phosphite and the like. Examples
of amines to form the amine salt of the above compounds may include: a mono-substituted
amine, a di-substituted amine or a tri-substituted amine represented by the following
formula (1). The alkyl group or the alkenyl group having 3 to 30 carbon atoms represented
by R in the formula (1) may be linear, branched or cyclic.
RnNH3-n (1)
In the formula: R represents an alkyl group or an alkenyl group having 3 to 30 carbon
atoms, preferably 4 to 18 carbon atoms, an aryl group or an arylalkyl group having
6 to 30 carbon atoms, preferably 6 to 15 carbon atoms, or a hydroxyalkyl group having
2 to 30 carbon atoms, preferably 2 to 18 carbon atoms; and n represents 1, 2 or 3.
When plural units ofR are contained, the plural units ofR may be mutually the same
or different.
[0014] Examples of the mono-substituted amine may include: a butyl amine, a pentyl amine,
a hexyl amine, a cyclohexyl amine, an octyl amine, a lauryl amine, a stearyl amine,
an oleyl amine, a benzyl amine and the like. Examples of the di-substituted amine
may include: a dibutyl amine, a dipentyl amine, a dihexyl amine, a dicyclohexyl amine,
a dioctyl amine, a dilauryl amine, a distearyl amine, an dioleyl amine, a dibenzyl
amine, a stearyl monoethanol amine, a decyl monoethanol amine, a hexyl monopropanol
amine, a benzyl monoethanol amine, a phenyl monoethanol amine, tolyl monopropanol
and the like. Examples of the tri-substituted amine may include: a tributyl amine,
a tripentyl amine, a trihexyl amine, a tricyclohexyl amine, a trioctyl amine, a trilauryl
amine, a tristearyl amine, a trioleyl amine, a tribenzyl amine, a dioleyl monoethanol
amine, a dilauryl monopropanol amine, a dioctyl monoethanol amine, a dihexyl monopropanol
amine, a dibutyl monopropanol amine, an oleyl diethanol amine, a stearyl dipropanol
amine, a lauryl diethanol amine, an octyl dipropanol amine, a butyl diethanol amine,
a benzyl diethanol amine, a phenyl diethanol amine, a tolyl dipropanol amine, a xylyl
diethanol amine, a triethanol amine, a tripropanol amine, a tertiary dodecyl amine
and the like.
Among the phosphorous extreme pressure agents, tricresyl phosphate and a diethyl hydrogen
phosphite tertiary dodecyl amine salt are preferable in perspective of heat resistance.
In view of blending effects and an economical aspect, a content of the extreme pressure
agent is typically approximately 0.01 to 30 mass% of the total amount of the lubricating
oil composition, preferably 0.01 to 10 mass%.
[0015] Antioxidants typically used for a lubricating oil such as an amine compound, a phosphorous
compound, a sulfur compound, a phosphorous/sulfur containing compound and a phenol
compound can be used as the antioxidant. Examples of the amine compound may include:
a monoalkyldiphenylamine compound such as monooctyldiphenylamine and monononyldiphenylamine;
a dialkyl diphenylamine compound such as 4,4'-dibutyldiphenylamine, 4,4'-dipentyldiphenylamine,
4,4'-dihexyldiphenylamine, 4,4'-diheptyldiphenylamine, 4,4'-dioctyldiphenylamine and
4,4'-dinonyldiphenylamine; a polyalkyldiphenylamine compound such as tetrabutyldiphenylamine,
tetrahexyldiphenylamine, tetraoctyldiphenylamine and tetranonyldiphenylamine; and
a naphthylamine compound such as α-naphthylamine, phenyl-α-naphthylamine, butylphenyl-α-naphthylamine,
pentylphenyl-α-naphthylamine, hexylphenyl-a-naphthylamine, heptylphenyl-a-naphthylamine,
octylphenyl-α-naphthylamine, nonylphenyl-α-naphthylamine, decylphenyl-α-naphthylamine,
dodecylphenyl-α-naphthylamine and the like.
[0016] Examples of the phosphorous compound, sulfur compound and phosphorous/sulfur containing
compound may include: the phosphorous compound such as diethyl[[3,5-bis(1,1-dimethylethyl)-4-hydroxyphenyl]methyl]phosphonate,
zinc dialkyldithiophosphate such as zinc di-2-ethylhexyldithiophosphate, 2,6-di-tert-butyl-4-(4,6-bis(octylthio)-1,3,5-triazine-2-ylamino)phenol,
a thioterpene compound such as a reactant of phosphorous pentasulfide and pinene,
dialkyl thiodipropionate such as dilauryl thiodipropionate and distearyl thiodipropionate.
Examples of the phenol compound may include: alkyl phenols such as 2,6-di-tert-butyl-4-methylphenol
and bisphenols such as methylene-4,4-bis(2,6-di-tert-butyl-4-methylphenol).
Among the antioxidants, diethyl[[3,5-bis(1,1-dimethylethyl)-4-hydroxyphenyl]methyl]phosphonate
is preferable in perspective of heat resistance.
A content of the antioxidant is typically approximately 0.01 to 10 mass% of the total
amount of the lubricating oil composition, preferably 0.03 to 5 mass%.
[0017] The composition, which is preferably formed of the above-described base oil and various
additives, has a kinematic viscosity (according to JIS (Japanese Industrial Standard)
K 2283) of 5 mm
2/s or less at 100 degrees C, preferably 4.95 mm
2/s or less, more preferably 4.5 mm
2/s or less. When the kinematic viscosity at 100 degrees C exceeds 5 mm
2/s, the driving power of the rotary gas compressor is excessive.
A flash point of the composition (according to C.O.C, JIS K 2265) is 200 degrees C
or more, preferably 210 degrees C or more, more preferably 220 degrees C or more.
When the flash point is less than 200 degrees C, there is an increasing danger of
flashing in operation of the rotary gas compressor filled with the composition.
5 volume % distillation temperature of the composition (according to JIS K 2254) is
350 degrees C or more, preferably 370 degrees C or more, more preferably 390 degrees
C or more. In case where 5 volume % distillation temperature is less than 350 degrees
C, lubricating oil consumption unpreferably increases when the rotary gas compressor
is operated for long hours.
The rotary gas compressor filled with the above composition as a lubricating oil consumes
less the lubricating oil and maintains a sufficient lubricity, thereby exhibiting
an excellent energy-saving effect. Particularly, when the composition is filled in
an oil-cooling screw compressor, the composition exhibits considerably excellent cooling
performance and heat resistance.
The kinematic viscosity of the composition at 40 degrees C is preferably 28 mm
2/s or less, more preferably 25 mm
2/s or less, more preferably 23 mm
2/s or less. When the kinematic viscosity at 40 degrees C exceeds 28 mm
2/s, the driving power of the rotary gas compressor is excessive.
[0018] The lubricating oil composition for the rotary gas compressor according to the aspect
of the invention may be further added with an oiliness agent, a rust inhibitor, a
detergent dispersant, a metal deactivator and an antifoaming agent as needed.
The oiliness agent may be exemplified by an aliphatic alcohol, a fatty acid compound
such as a fatty acid and a fatty acid metal salt, an ester compound such as a polyol
ester, a sorbitan ester and a glyceride and an amine compound such as an aliphatic
amine. The ester compound is preferable among these compounds since the ester compound
can provide both heat resistance and lubricity.
In view of blending effects, a content of the oiliness agent is typically approximately
0.1 to 30 mass% of the total amount of the lubricating oil composition, preferably
0.5 to 10 mass%.
[0019] The rust inhibitor may be exemplified by a metal sulfonate, aliphatic amines, an
organic phosphite ester, an organic phosphate ester, an organic metal sulfonate, an
organic metal phosphate, an alkenyl succinic acid ester, a multivalent alcohol ester
and the like. In view of blending effects, a content of the rust inhibitor is typically
approximately 0.01 to 10 mass% of the total amount of the lubricating oil composition,
preferably 0.05 to 5 mass%.
[0020] The detergent dispersant may be exemplified by a metal sulfonate, a metal salicylate,
a metal phenate, a metal phosphonate and succinimide. A metallic detergent dispersant
is preferable among these in perspective of detergent dispersivity and demulsification
performance.
In view of blending effects, a content of the detergent dispersant is typically approximately
0.1 to 30 mass% of the total amount of the lubricating oil composition, preferably
0.5 to 10 mass%.
[0021] The metal deactivator may be exemplified by benzotriazoles and thiadiazoles. In view
of blending effects, a content of the metal deactivator is typically approximately
0.01 to 10 mass% of the total amount of the lubricating oil composition, preferably
0.01 to 1 mass%.
The antifoaming agent may be exemplified by methyl silicone oil, fluorosilicone oil
and polyacrylates. In view of blending effects, a content of the antifoaming agent
is typically approximately 0.0005 to 0.01 mass% of the total amount of the lubricating
oil composition.
Examples
[0022] The invention will be further described in detail below with reference to Examples
and Comparatives, which by no means limit scope of the invention.
[Examples 1 to 6 and Comparatives 1 and 2]
[0023] Additives were added to predetermined base oils (API classification groups I to IV)
to prepare lubricating oil compositions having respective properties. Maximum loading
capacity, wear resistance, evaporation amounts and actual power consumption were evaluated.
A method of examining properties of the lubricating oil compositions and a method
for evaluating respective properties are shown below. Results are shown in Table 1.
(1) Properties of Lubricating Oil Composition
[0024] A method of examining each property (standard) is shown below.
(1.1) Kinematic Viscosity (100 degrees C, 40 degrees C): according to JIS K 2283
(1.2) Viscosity Index: according to JIS K 2283
(1.3) Density (at 15 degrees C): according to JIS K 2249
(1.4) Flash Point (C.O.C): according to JIS K 2265
(1.5) Distillation Property (5 volume % distillation temperature, 10 volume % distillation
temperature): according to JIS K 2254 (Distillation was conducted at reduced pressure
of 133MPa and an obtained value was converted to a value at atmospheric pressure.)
(2) Evaluation Items and Evaluation Method
[0025]
(2.1) Maximum Loading Capacity Test (Shell EP Test)
A test was conducted at a rotational speed of 1,800 rpm and at room temperature according
to ASTM D2783. A load wear index (LWI) was obtained from a last non-seisure load (LNL)
and a weld load (WL). The larger this value is, the better a load resistance is.
(2.2) Wear Resistance Test (Shell Wear Test)
A test was conducted under conditions of a load of 392N, a rotational speed of 1,200
rpm, an oil temperature of 80 degrees C and a testing time of 60 minutes according
to ASTM D2783. An average wear track diameter was calculated by averaging wear track
diameters of three half-inch balls.
(2.3) Film Residue Test
In a vessel based on JIS K 2540, a sample of 1g was filled. Air was flowed into the
vessel under an atmosphere at a constant temperature of 150 degrees C with a flowing
volume of 10 L/h for 6 hours. After the test, a mass of the sample (evaporation residue)
was measured. An amount of the evaporation residue relative to the original amount
of the sample was expressed by mass percentage.
(2.4) Actual Power Consumption
A commercially available oil-cooling screw compressor (motor output: 22kW, oil quantity:
10L, intake gas: air, intake pressure: atmospheric pressure, intake temperature: 25
degrees C) was used as a rotary gas compressor to measure effective power consumption
of the compressor motor when continuously operated for three hours at an average oil
temperature of 80 degrees C. The measurement was conducted by a clamp-on-sensor type
power meter that is commercially available.
The measurement was conducted in two operation modes as follows.
Operation Mode I: discharge pressure of 0.65 MPa
Operation Mode II: discharge pressure of 0.24 MPa
[0026]
[Table 1]
| |
Example 1 |
Example 2 |
Example 3 |
Example 4 |
Example 5 |
Example 6 |
Comparative 1 |
Comparative 2 |
| base oil (mass%) |
API GII (100 neutral) |
remnant |
|
|
remnant |
remnant |
remnant |
|
|
| API GIII (100 neutral) |
|
remnant |
|
|
|
|
|
|
| API GIV (100 neutral) |
|
|
remnant |
|
|
|
|
|
| API GII (150 neutral) |
|
|
|
|
|
65 |
remnant |
|
| API GI (100 neutral) |
|
|
|
|
|
|
|
remmant |
| additives (mass%) |
dioctyldiphenylamine |
2 |
2 |
2 |
2 |
2 |
2 |
2 |
2 |
| octylphenyl-α-naphthylamirte |
1 |
1 |
1 |
1 |
1 |
1 |
1 |
1 |
| phosphorous containing antioxidant *1 |
0.5 |
0.5 |
0.5 |
0.5 |
0.5 |
0.5 |
0.5 |
0.5 |
| ester oiliness agent *2 |
- |
- |
- |
- |
10 |
- |
- |
- |
| tricresyl phosphate |
- |
- |
- |
0.4 |
- |
- |
- |
- |
| amine salt of phosphate ester |
- |
- |
- |
0.02 |
- |
- |
- |
- |
| other additives *3 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
0.2 |
| properties |
kinematic viscosity (100 °C)(mm2/s) |
4.284 |
4.230 |
3.900 |
4.291 |
4.300 |
4.931 |
5.346 |
4.208 |
| kinematic viscosity (40 °C)(mm2/s) |
20.44 |
19.57 |
17.50 |
20.51 |
20.30 |
26.58 |
30.98 |
20.54 |
| viscosity index |
116 |
122 |
120 |
116 |
120 |
110 |
105 |
108 |
| density (15 °C)(g/cm3) |
0.8428 |
0.8338 |
0.8190 |
0.8431 |
0.8482 |
0.8558 |
0.8630 |
0.8577 |
| flash point (COC) (°C) |
212 |
230 |
222 |
212 |
215 |
218 |
222 |
210 |
| distillation property - 5 volume % distillation temperature (° C) |
375 |
398 |
417 |
376 |
377 |
375 |
374 |
346 |
| distillation property - 10 volume % distillation temperature (° C) |
388 |
406 |
422 |
388 |
390 |
390 |
393 |
351 |
| evaluation |
Shell EP LWI (N) |
165 |
171 |
164 |
301 |
307 |
163 |
164 |
170 |
| Shell wear (mm) |
0.58 |
0.59 |
0.56 |
0.31 |
0.33 |
0.59 |
0.57 |
0.55 |
| film residue (mass%) |
89.9 |
92.0 |
95.5 |
90.2 |
93.4 |
88.6 |
87.1 |
75.5 |
| actual power consumption-operation mode I (kWh) |
67.731 |
67.647 |
67.136 |
67.741 |
67.756 |
68.730 |
69.280 |
67.613 |
| actual power consumption - operation mode II (kWh) |
28.320 |
28.255 |
27.820 |
28.330 |
28.341 |
29.161 |
29.631 |
29.225 |
*1 diethyl[[3,5-bis(1,1-dimethylethyl)-4-hydroxyphenyl]methyl]phosphonate
*2 trimethylol propane trialkyl ester (in which an alkyl group is a mixture of C8
and C10)
*3 a package of a metallic detergent dispersant, metallic rust inhibitor and antifoaming
agent |
[Evaluation Results]
[0027] As shown in Table 1, the results of Examples 1 to 6 using the composition exhibited
excellent lubricity performance as a lubricating oil as well as excellent energy-saving
effect and consumed less lubricating oil. In contrast, in Comparative 1, a kinematic
viscosity at 100 degrees C is high and power consumption of a rotary gas compressor
is large. Moreover, a consumption of a lubricating oil is rather large irrespective
of the high kinematic viscosity at 100 degrees C. In Comparative 2, a consumption
of a lubricating oil becomes excessive due to a low 5 volume % distillation temperature,
thereby making it difficult to operate a rotary gas compressor for long hours.
Industrial Applicability
[0028] The present invention is preferably applicable as a lubricating oil for a rotary
gas compressor.