Microgels In Non-Crosslinkable Organic Media

Information

  • Patent Application
  • 20080064768
  • Publication Number
    20080064768
  • Date Filed
    September 23, 2004
    20 years ago
  • Date Published
    March 13, 2008
    16 years ago
Abstract
The invention relates to a composition which comprises a specific non-crosslinkable medium and at least one microgel, processes for its preparation, uses of the compositions, and microgel-containing polymers, rubbers, lubricants, coatings etc. prepared therefrom
Description
EXAMPLES
Example 1
SBR Gel in Nynas T110

In Example 1 described in the following, it is shown that compositions according to the invention which display particular rheological characteristics, such as structural viscosity, thixotropy and approximately Newtonian flow properties, are obtained using microgels based on SBR.


The use of the composition according to the invention as a functional and/or rheological additive, inter alia, emerges from this. Microgels which have little influence on the viscosity, that is to say in a first approximation show Newtonian flow properties, have favourable prerequisites for the use of the mixtures according to the invention in rubber or plastic. Microgels which greatly influence the viscosity, that is to say show structural viscosity or thixotropy flow properties, are suitable in particular for use of the mixtures according to the invention in greases.


The composition is shown in the following table:


















1. Nynas T 110
80%



2. Micromorph 1P or 5P
20%



Total
100%










Nynas T 110 is a hydrogenated naphthenic oil from Nynas Naphthenics AB.


Micromorph 5 P is a crosslinked rubber gel having an OH number of 4 based on SBR from RheinChemie Rheinau GmbH. Micromorph 5 P comprises 40 wt. % styrene, 57.5 wt. % butadiene and 2.5 wt. % dicumyl peroxide.


Micromorph 1 P is a crosslinked, surface-modified rubber gel based on SBR from RheinChemie Rheinau GmbH. Micromorph 1 P comprises 80 wt. % styrene, 12 wt. % butadiene, 5 wt. % ethylene glycol dimethacrylate (EGDMA) and 3 wt. % hydroxyethyl methacrylate (HEMA).


The characteristic data of the SBR gels are summarized in Table 1.









TABLE 1







Properties of the microgels Micromorph 1P and 5P.

















Gel
OH
Acid













Gel
D50
Tg
content
number


Product
type
[nm]
[° C.]
[wt. %]
[mg KOH/gpol.]
















Micromorph 1P
SBR
69
56
96
41
0.4


Micromorph 5P
SBR
50
none
92
 4
0.7










The abbreviations in the table have the following meanings:


DCP: Dicumyl Peroxide



  • d50: The diameter d50 is defined according to DIN 53 206 as the mean. In this case it is the average particle diameter of the particles in the latex. The particle diameter of the latex particles was determined here by means of ultracentrifugation (W. Scholtan, H. Lange, “Bestimmung der TeilchengröBenverteilung von Latices mit der Ultrazentrifuge”, Kolloid-Zeitschrift und Zeitschrift für Polymere (1972) volume 250, issue 8). The diameter values in the latex and for the primary particles in the compositions according to the invention are practically the same, since the particle size of the microgel particles does not change during the preparation of the composition according to the invention.



Tg: Glass Transition Temperature



  • For the determination of Tg and ΔTg, the DSC-2 apparatus from Perkin-Elmer is used.



Swelling Index QI



  • The swelling index QI was determined as follows:

  • The swelling index is calculated from the weight of the solvent-containing microgel swollen in toluene at 23° for 24 hours and the weight of the dry microgel:







Qi=wet weight of the microgel/dry weight of the microgel.

  • To determine the swelling index, 250 mg of the microgel are swollen in 25 ml toluene for 24 h, while shaking. The (wet) gel swollen with toluene is weighed, after centrifugation at 20,000 rpm, and then dried to constant weight at 70° C. and weighed again.


OH Number (Hydroxyl Number)



  • The OH number (hydroxyl number) is determined in accordance with DIN 53240 and corresponds to the amount of KOH in mg which is equivalent to the amount of acetic acid which is liberated during acetylation of 1 g of substance with acetic anhydride.



Acid Nnumber



  • The acid number is determined in accordance with DIN 53402 as already mentioned above and corresponds to the amount of KOH in mg which is necessary to neutralize one g of the polymer.



Gel Content

The gel content corresponds to the content which is insoluble in toluene at 23° C. The gel content is given by the quotient of the dried residue and the amount weighed out and is stated in percent by weight.


Preparation Example 1 for Micromorph 1 P

Micromorph 1 P is a microgel based on hydroxyl-modified SBR, prepared by direct emulsion polymerization using the crosslinking comonomer ethylene glycol dimethacrylate.


325 g of the Na salt bf a long-chain alkylsulfonic acid (330 g Mersolat K30/95 from Bayer AG) and 235 g of the Na salt of methylene-bridged naphthalenesulfonic acid (Baykanol PQ from Bayer AG) are dissolved in 18.71 kg water and the solution is initially introduced into a 40 I autoclave. The autoclave is evacuated and charged with nitrogen 3 times. Thereafter, 8.82 kg styrene, 1.32 kg butadiene, 503 g ethylene glycol dimethacrylate (90% pure), 314 g hydroxyethyl methacrylate (96%) and 0.75 g hydroquinone monomethyl ether are added. The reaction mixture is heated up to 30° C., while stirring. An aqueous solution consisting of 170 g water, 1.69 g ethylenediaminetetraacetic acid (Merck-Schuchardt), 1.35 g iron(II) sulfate*7H2O, 3.47 g Rongalit C (Merck-Schuchardt) and 5.24 g trisodium phosphate*12H2O is then metered in. The reaction is started by addition of an aqueous solution of 2.8 g p-menthane hydroperoxide (Trigonox NT 50 from Akzo-Degussa) and 10.53 g Mersolat K 30/95, dissolved in 250 g water. After a reaction time of 5 hours, the mixture is post-activated with an aqueous solution consisting of 250 g water, in which 10.53 g Mersolat K30/95 and 2.8 g p-menthane hydroperoxide (Trigonox NT 50) are dissolved. When a polymerization conversion of 95-99% is reached, the polymerization is stopped by addition of an aqueous solution of 25.53 g diethylhydroxylamine, dissolved in 500 g water. Thereafter, unreacted monomers are removed from the latex by stripping with steam. The latex is filtered and, as in Example 2 of U.S. Pat. No. 6,399,706, stabilizer is added and the product is coagulated and dried.


Micromorph 5 P is prepared analogously. The dry microgel powders Micromorph 1 P and Micromorph 5 P further processed according to the invention were obtained from the latex by spray drying.


For the preparation of the composition according to the invention, Nynas T 110 was initially introduced into the preparation vessel and Micromorph 5 P was added, while stirring by means of a dissolver. The composition was passed through the homogenizer four times under 950 bar.


The laboratory high-pressure homogenizer APV1000 from Invensys was used as the homogenizer.


The rheological properties of the composition were determined with a rheometer, MCR300, from Physica. A plate-cone system, CP25-1, was used as the measuring body. The measurements were carried out at 20° C.


Some measurement results for the composition of 80% Nynas T 110 and 20% Micromorph 1 P and Micromorph 5 P are shown in the following Table 2.


The greases Li-12OH, a semi-finished product, and E301 (15%), a laboratory product from RheinChemie Rheinau GmbH, were also measured as a comparison.


The viscosities η, which were measured at shear rates v′ of 5 s−1, 100 s−1, 1,000 s−1, 3,000 s−1 and 0,1 s−1, are shown in the table. The measurement was carried out with a measurement programme in which the measurement values (dynamic viscosities η etc.) were recorded in the sequence given above. The quotient η (v′=0.1 s−1)/η (v′=3,000 s−1) was defined as an arbitrary measure of the viscosity-increasing action of the microgel.


The composition of 80% Nynas T 110 and 20% Micromorph 5 P, which was passed through the homogenizer four times under 950 bar, shows rheological properties comparable to those of Li-120H AK33 or E301, i.e. Micromorph 5 P is suitable as a raw material for the preparation of greases.


The values in Table 2 show very clearly what diverse rheological properties can be achieved with the microgels.









TABLE 2







Rheological characterization of Mikromorph 1P and 5P


(in each case 20 wt. %) in Nynas T 110; 20° C.; cone-plate: CP 25-1.

















η
η
η
η
η
η (v′ = 0.1 s−1)/




Charac-
v′ = 5 s−1
v′ = 100 s−1
v′ = 1,000 s−1
v′ = 3,000 s−1
v′ = 0.1 s−1
η (v′ = 3,000 s−1)


Name
teristics
[Pas]
[Pas]
[Pas]
[Pas]
[Pas]
[]
Comments


















Li-120H
0.0935 s−1
375
23.3
3.9

7,950
2,0233)
Example grease without



instead of






additive (semi-finished



0.1 s−1






product) structural










viscosity, not very










thixotropic


E301 (15%)
0.15 s−1
83
14.6
6.6

2,420
 3683)
Example grease



instead of






without additive;



0.1 s−1






structural viscosity










in mineral oil


AE25648/51)
M. 1P/
23.4
5.1
3.45
2.3
1350
391




0 × 950 bar









AE25648/51)
M. 1P/
1.81
1.42
1.24
1.11
5.9
5
almost Newtonian flow



1 × 950 bar






properties


AE25648/51)
M. 1P/
2.3
1.77
1.34
1.20
1.99
1.5
almost Newtonian flow



2 × 950 bar






properties


AE25648/51)
M. 1P/
3.9
2.01
1.42
1.25
1.72
1.2
slightly thixotropic



3 × 950 bar









AE25648/51)
M. 1P/
9.3
2.80
1.71
1.46
3.3
2
thixotropic



4 × 950 bar









AE25648/62)
M. 5P/
6.8
1.94
1.56
1.38
2.02
1.3




0 × 950 bar









AE25648/62)
M. 5P/
11.9
5.4
3.8
2.44
2150
563
structural viscosity



1 × 950 bar









AE25648/62)
M. 5P/
19.6
6.0
3.6
2.34
1750
489
structural viscosity



2 × 950 bar









AE25648/62)
M. 5P/
33
6.8
3.6
2.36
1580
444
structural viscosity



3 × 950 bar









AE25648/62)
M. 5P/
57
7.7
3.6
2.40
1720
475
structural viscosity,



4 × 950 bar






not very thixotropic






1)20 wt.% Micromorph 5P in Nynas T 110




2)20 wt.% Micromorph 5P in Nynas T 110




3)η(v′ = 0.1 s−1)/ηv′ = 1,000 s−1)







The values measured show a thickening which, with suitable choice of the microgel/lubricant combination from the point of view of rheology, surprisingly allows the preparation of lubricating greases.


Moreover, rheological properties can be controlled with microgels in the liquid media described. The compositions according to the invention are of particular interest as thickeners, as agents for preventing running and settling out and as a rheological additive.


The compositions described or similar compositions can advantageously be used in lubricating greases, lacquers and paints, adhesives, rubber, plastics and gel coats or thermoplastic elastomers.


The compositions prepared in Example 1 can be used particularly advantageously in lubricating greases. In these, they lead to particularly favourable properties, such as a high thixotropy or structural viscosity.


Further very advantageous properties which are co-introduced into the particular systems via the microgels can be seen from the following examples.


Example 2
Transparency and Phase Separation As Well As Rheological and Tribological Properties of the Lubricants From the Combination of 2% Microgel—Lubricating Oil

In Example 2 described in the following, it is shown that compositions according to the invention which display particular characteristics in respect of transparency and stability towards separation are obtained using microgels based on SBR and NBR.


The composition is shown in the following table:


















1. Lubricating oil
98%



2. Microgel
2%



Total
100%










Shell Catenex S 932 is a paraffinic, highly refined mineral oil from Deutsche Shell GmbH.


Shell Gravex 921 is a hydrogenated, naphthene-based manufactured oil from Shell&DEA Oil GmbH.


Methyl Ester SU is a methyl ester (Radia 7961) from Oleon NV.


Silicone Oil M350 is a polydimethylsiloxane from Bayer MaterialScience AG.


Baylube 68CL is a polyether from RheinChemie Rheinau GmbH.


The microgels OBR 1210 and OBR 1212 are crosslinked, surface-modified rubber gels based on SBR from RheinChemie Rheinau GmbH. Micromorph 4 P is a crosslinked rubber gel which is not surface-modified and is based on SBR, from RheinChemie Rheinau GmbH.


OBR 131OD is a crosslinked, surface-modified rubber gel based on NBR (Tab. 3). The microgels are prepared by a procedure analogous to that described in Example 1 for Micromorph 1 P.









TABLE 3







Composition of the microgels OBR 1210, OBR 1212,


OBR 1310D and Micromorph 4P.

















TMP




Name
Acrylonitrile
Butadiene
Styrene
TMA
HEMA
Comments
















OBR 1210
0
51.6
34.4
12.5
1.5



OBR 1212
0
46.5
31
12.5
10



OBR 1310D
23.8
61.2
0
5
10



Micromorph





As Micromorph


4P





5P; but 1.5








DCP1)









The characteristic data of the SBR gels and of the NBR gel are summarized in Table 4.









TABLE 4







Properties of OBR 1210, OBR 1212, OBR 1310D and


Micromorph 4P.









Analytical data



























Tg












level










OH

DSC/






Particle



number
Acid
2nd



Gel
D50
SAspec.
density
Tg
Gel

[mg
num-
htg up


Microgel
type
[nm]
[m2/g]
[g/ml]
[° C.]
[wt. %]
QI
KOH/g]
ber
[° C.]




















OBR 1210
SBR
60
102
0.993
−20.0
95.4
4.9
4
1.1



OBR 1212
SBR
55
107
1.017
−5.0
99.2
4.4
42
1.7



OBR 1310
NBR
78
 80
0.992
−25.0
99.4
4.9
32
1.3
11.0


D












Micromorph
SBR
57
111

−15.0
94.6
9.0
8
6



4P










The abbreviations in the table have the following meanings:
  • SAspec.: specific surface area in m2/g


Glass Transition Range:



  • The glass transition range was determined as described above. Otherwise see Example 1.



Control of the Homogeneity:



  • The samples were tested visually for separation one week after the preparation.



Control of the Transparency:



  • The transparency of the samples was checked visually. Samples which showed separation or flocculation were stirred up before the evaluation.



Preparation of the Compositions According to the Invention

For the preparation of the composition according to the invention, the particular lubricating oils were initially introduced into the preparation vessel and the particular microgel was added, while stirring by means of a dissolver. The mixture was left to stand for at least one day, and then further processed with the homogenizer. The composition according to the invention was introduced into the homogenizer at room temperature and passed through the homogenizer six times in batch operation under 900 to 1,000 bar. During the first pass the microgel paste heats up to approx. 40° C., and during the second pass to approx. 70° C. Thereafter, the microgel paste was cooled down to room temperature by being left to stand, and the operation was repeated until six passes had been achieved.


The rheological properties of the composition were determined with a rheometer, MCR300, from Physica. A plate-cone system, CP 50-2, was used as the measuring body. The measurements were carried out at 40° C.


Some measurement results for the microgels described above are shown in the following Table 5 to 7.









TABLE 5







Clouding and separation of the microgel-containing


lubricating oils (2% microgel): room temperature.











Lubricating



Phase


oil
Microgel
Dispersing
Clouding
separation





Shell
OBR 1212
6 x
milky-
no settling


Catenex


cloudy


S932



OBR 1310D
6 x
moderately
severe





transparent
settling



Micromorph
6 x
milky-
severe



4P

cloudy
settling


Shell
OBR 1210
6 x
milky-
severe


Gravex 921


cloudy
settling



OBR 1310D
6 x
cloudy/moderately
severe





transp.
settling



Micromorph
6 x
milky-
no settling



4P

cloudy


Methyl
OBR 1210
6 x
very weakly
no settling


Ester SU


transparent



OBR 1212
6 x
milky-
no settling





cloudy



OBR 1310D
6 x
milky-
moderate





cloudy
settling



Micromorph
6 x
milky-
no settling



4P

cloudy


Silicone Oil
OBR 1210
6 x
milky-
no settling


M350


cloudy



OBR 1310D
6 x
milky-
severe





cloudy
settling



Micromorph
6 x
milky-
no settling



4P

cloudy









From Tab. 5 it can be seen that there are many compositions according to the invention which on the one hand are based on different lubricating oils and on the other hand do not settle out. In particular, Micromorph 4 P shows no settling out in any combination. This is surprising, since only 2 wt. % microgel was added.


Furthermore, a composition which is largely transparent and does not separate, namely OBR 1210 in Methyl Ester SU, was found.









TABLE 6







Rheological characterization of the microgel-containing


lubricating oils; 40° C.; cone-plate: measurement


system CP 50-2.

















Vis.
Vis.
Quotient





Vis.
(40° C.;
(40° C.;
Vis.(5s−1)/





(40° C.;
1,000
3,000
Vis. (3,000




Homoge
5 s−1)
s−1)
s−1)
s−1)


Binder
Microgel
nization
[mPas]
[mPas]
[mPas]
[mPas]
















Methyl Ester

0x
1.83
3.9
5.3
0.35


SU








Methyl Ester
OBR1310D
6x
23.8
5.9
6.4
3.7


SU
(2%)







Methyl Ester
Micromorph
6x
83.8
9.5
8.3
10.


SU
4P (2%)







Shell Cate-

0x
55
54
53
1.0


nex S932








Shell Cate-
0BR1212
6x
107
64
60
1.8


nex S932
(2%)







Shell Gravex

0x
19.8
21
21
0.9


921








Shell Gravex
Micromorph
6x
118
34
30
4.0


921
4P (2%)







Silicone Oil
BR1210
6x
269
244
238
1.1


M350
(2%)









From the values of Table 6, the rheological action of the microgels even at a concentration of two percent can be clearly seen; nevertheless, there is a clear differentiation into Newtonian, structural viscosity and thixotropic flow properties. OBR 1210 has Newtonian flow properties in Silicone Oil M350.


SRV tests were furthermore carried out for determination of the coefficient of friction (Tab. 7; FIGS. 2a and 2b). The SRV tests were carried out by the method of ASTM 5706-97, a ring-plate geometry being chosen instead of a ball-plate geometry:












100 CR 6 steel ring lapped on 100 CR 6 steel plate


















Frequency:
50 Hz



Load:
300 N (vary as required)



Temperature:
100° C.



Amplitude:
1.500 mm



Duration:
60 minutes

















TABLE 7







SRV test on the combinations of 2 wt. % microgel (OBR


1210) - lubricating oil (Baylube 68CL) and of Baylube


68CL for


comparison; ring-plate.











Load: 300 N

Coef-




100CR6 steel ring/
Coefficient
ficient

Appearance


100CR6 steel plate,
of friction
of friction
Wear
of the


lapped
min
max
of plate
friction site





68CL-1210
0.025μ
0.087μ
cannot be
metallic





measured
blank


Baylube 68CL as a
0.044μ
0.081
cannot be
metallic


reference


measured
blank









It can be seen from Table 7 that for the composition according to the invention, OBR 1210/Baylube 68CL, a clearly lower coefficient of friction is found compared with the pure lubricating oil Baylube 68CL. It is moreover found that the course of the curve during measurement is smoother, which indicates that the microgels lead to a lower wear on the surface of the test plate.


The microgel, like many other microgels also, surprisingly has properties which reduce the coefficient of friction and can therefore be employed as a coefficient of friction modifier.


Example 3
Phase Separation and Rheological and Tribological Properties of the Lubricants from the Combination of 10%, 15%, 20% and 30% Microgel—Lubricating Oil

In Example 3 described in the following, it is shown that compositions according to the invention which display particular characteristics in respect of transparency and stability in respect of separation can be obtained using microgels based on SBR and NBR. It is furthermore found that lubricating greases can be obtained.


The composition of the microgel paste is shown in the following table:


















1. Lubricating oil
90%, 85%, 80%, 70%



2. Microgel
10%, 15%, 20%, 30%



Total
100%










Shell Catenex S 932 is a paraffinic, highly refined mineral oil from Deutsche Shell GmbH.


Methyl Ester SU is a methyl ester (Radia 7961) from Oleon NV.


Refined rapeseed oil is an oil from Cereol Deutschland GmbH, which is obtained from renewable raw materials.


Baylube 68CL is a polyether from RheinChemie Rheinau GmbH.


Nynas T 110 is a hydrogenated naphthenic oil from Nynas Naphthenics AB.


The microgels OBR 1210 and OBR 1212 are crosslinked, surface-modified rubber gels based on SBR from RheinChemie Rheinau GmbH. OBR 1135 and Micromorph 5 P are crosslinked rubber gels which are not surface-modified and are based on BR and SBR respectively, from RheinChemie Rheinau GmbH.


Micromorph 5 P is described in Example 1. The compositions of the microgels OBR 1210 and OBR 1212 are described in Example 2. OBR 1135 is a BR gel; it comprises 97.5% and 2.5% dicumyl peroxide. The microgels are prepared as described in Example 1 for Micromorph 1 P.


The greases Li-120H, a semi-finished product, and E301 (15%) and M10411, laboratory products from RheinChemie Rheinau GmbH, were also measured as a comparison.


The characteristic data of the microgels are summarized in Examples 1 and 2.


Preparation of the Compositions According to the Invention

The composition according to the invention was prepared as already described above. In deviation from this, an air pressure of 1 to 5 bar was required in certain cases to convey the material into the homogenizer. The number of passes is stated in the following.


The rheological properties of the composition were determined with a rheometer, MCR300, from Physica. A plate-cone system, CP 25-1, was used as the measuring body. The measurements were carried out at 20° C.


Some measurement results for the microgels described above are shown in the following (Tab. 8-10):


20 and 30% Micromorph 5 P/Nynas T110 exude little lubricating oil and are solid.


Only 30% OBR 1135 and OBR 1210/Nynas T110 exude little lubricating oil and are solid.


20% OBR 1135/rapeseed oil and 20Micromorph 5 P/rapeseed oil also show no separation on the surface, even after 1.5 years. Hardly any separation is also shown with 10% of the same gels in rapeseed oil.









TABLE 8







Rheological characterization of the microgel-containing


lubricating greases; 20° C.; cone-plate: measurement


system CP 25-1.



















Quotient





Vis.
Vis.
Vis.
Vis.(5s−1)/





(20° C.;
(20° C.;
(20° C.;
Vis.(1,000




Homogen-
5 s−1)
100 s−1)
1,000 s−1)
s−1)


Lubricating oil
Microgel
ization
[Pas]
[Pas]
[Pas]
[]
















Baylube 68CL
OBR1210
6x
172
20.4
5.7
30



(30%)







Shell Catenex
OBR1212
6x
22.6
4.2
1.4
16


S932
(30%)









  • The drop point, penetration and oil separation capacity were measured by the method of or in accordance with the particular standards:



DIN 51801: Drop Point:



  • The drop point describes that temperature at which the first drop emerges from the material to be determined and touches the base of the drop vessel.



DIN 51580: Penetration:



  • Penetration is understood as meaning the measurement of the consistency of paste-like or waxy-solid materials by means of penetration of a conical cone shell into the sample. The penetration depth in 1/10 mm is stated as the penetration value P.

  • On an untreated sample: Pu

  • On a milled sample: Pm,60 (after 60 strokes) or Pm,100,000 (after 100,000 strokes)



DIN 51817: Oil Separation:



  • The oil separation is a measure of the stability of the grease matrix of thickener and base liquid. The sample is weighted with a weight, for example, at 40° C. for a certain time. By this means, base liquid emerges from the grease matrix during the loading. The percentage content of base liquid after the loading time at the given temperature is determined.










TABLE 9







Physical properties of the combinations of 30%


microgel


(Micromorph 5P, OBR 1135, OBR 1210) - lubricating oil


(Baylube 68CL,


Methyl Ester SU, Nynas T 110, Shell Catenex S932)


and of PU grease


M10411 and Lithium 12OH grease for comparison.


Drop point, resting and milling penetration.












Penetration




Drop point
Pu/Pm 60
Penetration



(DIN 51801)
(DIN 51580)
Pm, 60.000



[° C.]
[1/10 mm]
[1/10 mm]














Li—12OH grease
186
188/190
241


Methyl Ester SU -
177
215/214
249


Micromorph 5P (30%)


Baylube 68CL -
174/137
238/247
238


OBR1210 (30%)


Nynas T110 - OBR
>280
180/191
196


1135 (30%)


Nynas T110 - PU

190/213
320


grease M 10411 (12%)









  • The oil separation capacity (18 h/40° C.) is the same for the composition according to the invention of Nynas T110-OBR 1135 (30%) and the lithium grease Li-12OH grease: 0.29% Low Pu and high Pm, 60,000 values are typical of greases. This is confirmed by the measurements on the lithium 12 grease and the PU grease, as can be seen from Tab. 9.

  • The microgel-lubricating oil combinations show little or no differences in the values for the resting penetration Pu and the milling penetration Pm, 60,000. Thus, the OBR 1210-Baylube 68CL combination in particular is stable to shearing forces.










TABLE 10







SRV test on the combinations of 30% microgel


(Micromorph 5P, OBR 1210) - lubricating oil (Baylube


68CL, Methyl Ester SU, Shell Catenex S932) and of PU


grease M10411 and lithium 12 grease for comparison.












Coef-





Load: 300 N
ficient
Coef-


100CR6 steel
of
ficient of


ring/100CR6
friction
friction
Wear


steel plate,
min
max
of plate
Appearance of the


lapped
[μm]
[μm]
[μm]
friction site














Li—12OH grease
0.020
0.230
2.84
metal. blank,


without add.



surrounding area


Fuchs (P 1031)



with much black






abrasion


Methyl Ester SU -
0.095
0.295
2.07
metal. blank,


Micromorph 5P



surrounding area


(30%)



black with furrows


Baylube 68CL -
0.045
0.080
cannot be
metal. blank,


OBR1210 (30%)


measured
surrounding area






without deposits


PU grease M
0.075
>0.40
5.92
friction site has


10411 (12%) in



eaten away spots


Nynas T110



and tribocorrosion






surrounding area






heavy black deposits









  • The course of the SRV curves shows the following: In contrast to the comparison greases, the OBR 1210 grease shows a smooth course of the curve, which ends at the lower level of the coefficient of friction, and a metallic blank friction site.










TABLE 11







Wear tests on the combinations of 30% microgel


(Micromorph 5P,


OBR 1210) - lubricating oil (Baylube 68CL, Methyl


Ester SU, Shell Catenex S932) and of PU grease


M10411 and lithium 12 grease for comparison.










FBA shock load




(by the method of
FBA goods/weld



DIN 51350; DIN
load



balls) 1,000 N,
(DIN 51350, part 4)



1,420 rpm, 1 min
1,420 rpm, 1 min













Li—12OH grease without
2.60 mm
+1,400/−1,500
N


add. Fuchs (P 1031)


Methyl Ester SU -
1.75 mm
+1,800/−1,900
N


Micromorph 5P (30%)


Baylube 680L - OBR1210
0.78 mm
+1,800/−1,900
N


(30%)


PU grease M 10411 (12%)
3.50 mm
<1,400
N


in Nynas T110









  • Table 11 shows that the shock load and FBA goods/weld load are improved significantly according to the invention. Example 3 shows that the compositions according to the invention having a relatively high content of microgel (15-30%) surprisingly show properties comparable to those of commercial greases (stability towards settling out, low separation of oil, consistency etc.) but more favourable properties (high shear stability, i.e. almost no change in the penetration values after milling with 60,000 strokes) and exceptionally high drop points such as are otherwise achieved only by heat-resistant greases, such as e.g. Pu greases or Ca complex greases. Furthermore these compositions display a positive action on coefficients of friction, which is completely untypical of standard greases.



Example 4
SBR Gel OBR 1312B, Modified by Hydroxyl Groups, in Baylube 68CL

In Example 4 described below, it is shown that, using microgels based on SBR which are modified by hydroxyl groups, compositions according to the invention which chiefly contain primary particles having an average particle diameter of approx. 43 nm can be prepared in a homogenizer by applying 900 to 1,000 bar with 2 to 6 passes.

  • The composition is shown in the following table:
















1.
Baylube 68CL
97.8


2.
OBR 1312B
2.0


3.
Dispersing auxiliary
0.2



Total
100.0









Baylube 68CL is a polyether from RheinChemie Rheinau GmbH.


The microgel OBR 1312B is a crosslinked, surface-modified rubber gel based on SBR from RheinChemie Rheinau GmbH (Tab. 12). The microgel is prepared analogously to Example 1 for Micromorph 1 P.









TABLE 12







Composition of the microgel OBR 1312B.















bu-








ta-








di-






Name
Acrylonitrile
ene
Styrene
TMPTMA
HEMA
Comments





OBR
0
46
42.5
1.5
10



1312B









The characteristic data of OBR 1312B are summarized in Table 13.









TABLE 13







Properties of OBR 1312B.


Analytical data



























Tg












level










OH

DSC/






Particle



number
Acid
2nd htg


Micro-
Gel
d50
SAspec.
density
Tg
Gel

[mg
num-
up


gel
type
[nm]
[m2/g]
[g/ml]
[° C.]
[wt. %]
QI
KOH/g]
ber
[° C.]





OBR
SBR
43
141
0.996

99.9
9.7
44
1.3



1312B




21.5









For the preparation of the composition according to the invention, Baylube 68CL was initially introduced into the preparation vessel and OBR 1312B was added, while stirring by means of a dissolver. The mixture was left to stand for at least one day, and then further processed with the homogenizer.


The composition according to the invention was introduced into the homogenizer at room temperature and passed through the homogenizer 6 times under 960 bar in batch operation. During the first pass the microgel paste heats up to approx. 40° C., and during the second pass to approx. 70° C. Thereafter, the microgel paste was cooled to room temperature and dispersed a third and fourth time. This was repeated until six passes had been achieved.


The particle diameter of the latex particles was -determined by means of ultracentrifugation (W. Scholtan, H. Lange, “Bestimmung der TeilchengröBenverteilung von Latices mit der Ultrazentrifuge”, Kolloid-Zeitschrift und Zeitschrift für Polymere (1972) volume 250, issue 8).


The particle size distributions of the original, not yet dried latex of the OBR 1312B microgel and of the OBR 1312B redispersed in Baylube 68CL (TZE 122) can be seen in the following figures.


It can be seen that, surprisingly, almost the entire amount of the dried and therefore agglomerated OBR powder has been successfully redispersed down to the primary particles, the average particle diameter of the redispersed mixture even being below the average particle diameter of the original latex. It is to be noted in addition that the measurement was carried out on a redispersed sample which had been stored for 6 months at room temperature, i.e. the dispersion surprisingly remained stable for 6 months.


Because of its low content of reagglomerated particles, the redispersed composition moreover is highly transparent.

Claims
  • 1. Composition comprising at least one non-crosslinkable organic medium (A) which has a viscosity of less than 30,000 mPas at a temperature of 120° C. and at least one microgel (B).
  • 2. Composition according to claim 1, wherein the non-crosslinkable organic medium (A) has a viscosity of less than 1,000 mPas at a temperature of 120° C.
  • 3. Composition according to claim 1, wherein the non-crosslinkable organic medium (A) has a viscosity of less than 200 mPas at a temperature of 120° C.
  • 4. Composition according to claims 1 to 3, characterized in that the primary particles of the microgel (B) have an approximately spherical geometry.
  • 5. Composition according to claims 1 or 4, characterized in that the deviation of the diameters of an individual primary particle of the microgel (B), defined as [(d1−d2)/d2]×100,wherein d1 and d2 are any two desired diameters of the primary particle and d1 is >d2, is less than 250%.
  • 6. Composition according to claim 5,-wherein the said deviation is less than 50%.
  • 7. Composition according to one of claims 1 to 6, characterized in that the primary particles of the microgel (B) have an average particle size of 5 to 500 nm.
  • 8. Composition according to one of claims 1 to 6, characterized in that the primary particles of the microgel (B) have an average particle size of less than 99 nm.
  • 9. Composition according to one of claims 1 to 8, characterized in that the microgels (B) have contents which are insoluble in toluene at 23° C. of at least about 70 wt. %.
  • 10. Composition according to one of claims 1 to 9, characterized in that the microgels (B) have a swelling index in toluene at 23° C. of less than about 80.
  • 11. Composition according to one of claims 1 to 10, characterized in that the microgels (B) have glass transition temperatures of −100° C. to +120° C.
  • 12. Composition according to one of claims 1 to 11, characterized in that the microgel (B) is a crosslinked microgel which is not crosslinked by high-energy radiation.
  • 13. Composition according to one of claims 1 to 12, characterized in that the microgels (B) have a width of the glass transition range of greater than about 5° C.
  • 14. Composition according to one of claims 1 to 13, characterized in that the microgels-(B) are obtainable by emulsion polymerization.
  • 15. Composition according to one of claims 1 to 14, characterized in that the microgel (B) is based on rubber.
  • 16. Composition according to one of claims 1 to 15, characterized in that the microgel (B) is based on homopolymers or random copolymers.
  • 17. Composition according to one of claims 1 to 16, characterized in that the microgel (B) is modified by functional groups which are reactive towards C═C double bonds.
  • 18. Composition according to one of claims 1 to 17, wherein the non-crosslinkable medium (A) is at least one compound which is chosen from the group which consists of solvents, saturated or aromatic hydrocarbons, polyether oils, naturally occurring and synthetic ester oils, polyether-ester oils, phosphoric acid esters, silicon-containing oils, halohydrocarbons and liquid renewable raw materials.
  • 19. Composition according to one of claims 1 to 18, which comprises 0.1 to 90 wt. % of the microgel (B), based on the total amount of the composition.
  • 20. Composition according to one of claims 1 to 19, characterized in that it comprises 10 to 99.9 wt. % of the non-crosslinkable organic medium (A).
  • 21. Composition according to one of claims 1 to 20, characterized in that it additionally comprises fillers and/or additives.
  • 22. Composition according to one of claims 1 to 21, characterized in that it has been prepared by mixing the non-crosslinkable medium (A) and the microgel (B) by means of a homogenizer, a bead mill (stirred ball mill), a triple-roll mill, a single- or multiple-screw extruder, a kneader, an Ultra-Turrax apparatus and/or a dissolver.
  • 23. Composition according to claim 22, characterized in that it has been prepared by means of a homogenizer, a bead mill (stirred ball mill), a triple-roll mill or a dissolver.
  • 24. Composition according to one of claims 1 to 23, characterized in that it has a viscosity of 2 mPas up to 50,000,000 mPas at a speed of 5 s−1, determined with a cone-plate measuring system in accordance with DIN 53018 at 20° C.
  • 25. Composition according to one of claims 1 to 24, characterized in that the microgel (B) has a swelling index in toluene at 23° C. of 1 to 15.
  • 26. Composition according to one of claims 1 to 25, characterized in that the microgels (B) have contents which are insoluble in toluene at 23° C. of at least 95 wt. %.
  • 27. Composition according to one of claims 1 to 26, characterized in that the microgel is not modified with hydroxyl groups.
  • 28. Composition according to one of claims 1 to 27, characterized in that the microgel is not modified.
  • 29. Use of the composition according to one of claims 1 to 28 for incorporation into thermoplastics, rubbers or thermoplastic elastomers.
  • 30. Use of the composition according to one of claims 1 to 28 for the preparation of microgel-containing polymers.
  • 31. Use according to claim 30 for the preparation of microgel-containing rubbers.
  • 32. Use according to claim 30 for the preparation of microgel-containing thermoplastic elastomers.
  • 33. Use of the compositions according to one of claims 1 to 28 for the preparation of lubricants, shaped articles or coatings.
  • 34. Use of the composition according to claim 33 for the preparation of lubricating greases or modified lubricating oils.
  • 35. Use of the compositions according to one of claims 1 to 28 as a additive for plastics, rubbers, coating compositions or lubricants.
  • 36. Use of microgels as a rheological additive, in particular as a thickener or thixotropic agent, in non-crosslinkable organic media which have a viscosity of less than 30,000 mPas at a temperature of 120° C.
  • 37. Plastics, rubbers, thermoplastic elastomers, coating compositions or lubricants comprising the compositions according to one of claims 1 to 28.
  • 38. Process for the preparation of the composition according to one of claims 1 to 28, characterized in that components (A) and (B) are subjected together to the treatment with a homogenizer, a bead mill, a triple-roll mill, a single- or multiple-screw extruder, a kneader and/or a dissolver.
  • 39. Process for the preparation of the composition according to one of claims 1 to 28, characterized in that components (A) and (B) are subjected together to the treatment with a homogenizer, a bead mill, a triple-roll mill and/or a dissolver.
Priority Claims (1)
Number Date Country Kind
103 44 975.2 Sep 2003 DE national
PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/EP04/52290 9/23/2004 WO 00 8/8/2007