process oils
process oils process oils
INTRODUCTION TO PROCESS OILS Krisda SUCHIVA Research and Development Centre for Thai Rubber Industry, Mahidol University
- Page 2 and 3: INTRODUCTION TO PROCESS OILS Proces
- Page 4 and 5: INTRODUCTION TO PROCESS OILS Functi
- Page 6 and 7: INTRODUCTION TO PROCESS OILS How do
- Page 8 and 9: INTRODUCTION TO PROCESS OILS Effici
- Page 10 and 11: PROCESS OILS Origin and Composition
- Page 12 and 13: PROCESS OILS Important Properties o
- Page 14 and 15: PROCESS OILS Important Properties o
- Page 16 and 17: PROCESS OILS 4. Loss of oil during
- Page 18 and 19: PROCESS OILS Polycyclic Aromatic Hy
- Page 20 and 21: PROCESS OILS Comparison of Differen
- Page 22 and 23: PROCESS OILS Comparison of Differen
- Page 24 and 25: PROCESS OILS Hardness, IRHD 70 Comp
- Page 26 and 27: PROCESS OILS Comparison of Differen
- Page 28 and 29: PROCESS OILS Performance of Low PAH
- Page 30 and 31: PROCESS OILS SUMMARY 5. Study on NR
INTRODUCTION TO PROCESS OILS<br />
Krisda SUCHIVA<br />
Research and Development Centre for Thai Rubber Industry,<br />
Mahidol University
INTRODUCTION TO PROCESS OILS<br />
Process <strong>oils</strong> are used in the rubber industry to,<br />
• improve the <strong>process</strong>ability of rubbers and rubber<br />
compounds<br />
<strong>process</strong> aids<br />
• increase the bulk of rubber in order to lower cost<br />
oil-extended rubbers<br />
Main application is <strong>process</strong> aid.<br />
2
INTRODUCTION TO PROCESS OILS<br />
Process aids are increasingly important for the rubber<br />
industry due to the following needs,<br />
- improve efficiency and productivity<br />
- lower energy consumption<br />
In total,<br />
- reduce production cost<br />
- improve product quality<br />
3
INTRODUCTION TO PROCESS OILS<br />
Functions of <strong>process</strong> aids,<br />
1. reduce viscosity<br />
2. reduce elasticity<br />
3. aid dispersion of fillers<br />
4. reduce power consumption<br />
Additional requirement<br />
1. do not affect intended properties of finished products<br />
2. act at low dosage level<br />
3. non-toxic<br />
4
INTRODUCTION TO PROCESS OILS<br />
Materials used as <strong>process</strong> aids,<br />
1. chemical peptizers<br />
2. fatty acid soaps<br />
3. fatty acid ester<br />
4. petroleum <strong>oils</strong><br />
5. factice<br />
6. resins<br />
7. partially vulcanised rubber<br />
8. liquid polymers<br />
9. waxes<br />
Process oil is just one of the <strong>process</strong> aids.<br />
5
INTRODUCTION TO PROCESS OILS<br />
How do <strong>process</strong> aids work ?<br />
For reduction of viscosity and elasticity<br />
2 Mechanisms,<br />
1. Lowering molecular weight of polymer<br />
peptizer<br />
• molecular entanglement reduced<br />
• easier flow of molecules<br />
Chemical <strong>process</strong>ing aids<br />
6
INTRODUCTION TO PROCESS OILS<br />
2. Lowering of intermolecular interactions<br />
<strong>process</strong> aid<br />
• flow of molecules become easier<br />
Most <strong>process</strong> aids work on this principle<br />
e.g. fatty acid soaps, fatty acid ester, <strong>oils</strong>, liquid polymers.<br />
No reduction in MW, hence the final properties not affected<br />
7
INTRODUCTION TO PROCESS OILS<br />
Efficiency of physical <strong>process</strong> aids depend on degree of miscibility<br />
with polymer or solubility in polymers.<br />
most efficient<br />
completely miscible<br />
or<br />
completely soluble<br />
partially miscible<br />
or<br />
partially soluble<br />
most effective in reducing<br />
viscosity<br />
only small amount is required.<br />
less efficient<br />
less effective in reducing<br />
viscosity<br />
Higher amount is required.<br />
immiscible<br />
or<br />
insoluble<br />
least efficient<br />
least effective in reducing<br />
viscosity<br />
large amount is required. 8
PROCESS OILS<br />
9
PROCESS OILS<br />
Origin and Composition of Process Oils<br />
• PROCESS OILS are derived from petroleum (crude oil) after the<br />
more volatile petrol and heating oil fractions have been removed by<br />
distillation.<br />
• PROCESS OILS are MIXTURES of paraffinic, naphthenic and<br />
aromatic compounds of wide distribution of molecular weight.<br />
Paraffinic <strong>oils</strong><br />
CH 3 CH 2 CH 2 CH 2 CH 2 CH 3 CHCH 2 CHCH 2 CH 3 CH 2<br />
paraffins<br />
isoparaffins<br />
CH 3 CH 3<br />
Naphthenic <strong>oils</strong><br />
Aromatic <strong>oils</strong><br />
derivatives of cyclohexane or decalin<br />
derivatives naphthalene, debenzothiophene,<br />
carbazole, etc.<br />
10
PROCESS OILS<br />
Type of Process Oils<br />
Type<br />
%<br />
paraffinic<br />
%<br />
naphthenic<br />
%<br />
aromatic<br />
VGC<br />
Paraffinic oil 60-74 20-35 0-10 0.790-0.819<br />
Naphthenic oil 35-45 30-45 10-30 0.850-0.899<br />
Aromatic oil 20-35 20-40 35-50 0.950-0.999<br />
11
PROCESS OILS<br />
Important Properties of Process Oils<br />
1. solubility or miscibility or compatibility with rubbers<br />
• Determine efficiency in reducing viscosity/flow characteristics<br />
• Depends on,<br />
- % Aromaticity : the higher, the more efficient<br />
- molecular weights (viscosity) : the smaller, the more<br />
efficient<br />
• High solubility means more oil can be incorporated into the<br />
rubber<br />
higher loading of oil possible.<br />
12
PROCESS OILS<br />
Important Properties of Process Oils<br />
• Level of aromaticity measured by<br />
1) VISCOSITY GRAVITY CONSTANT (VGC)<br />
G<br />
= 1.0752-a<br />
a<br />
specific gravity<br />
VGC<br />
10<br />
log(V+38)<br />
Viscosity (saybolt)<br />
High VGC = high aromaticity<br />
2) ANILINE POINT<br />
Aniline point = temperature at which equal volumes<br />
oil and aniline are mutually soluble.<br />
Low Aniline Point = high aromaticity<br />
note : ● Aniline point can be influenced by MW of oil.<br />
● Can be difficult to determine with very dark and opaque <strong>oils</strong>.<br />
13
PROCESS OILS<br />
Important Properties of Process Oils<br />
Compatibility of <strong>process</strong> <strong>oils</strong> with various rubbers<br />
Oil Type<br />
Rubbers<br />
NR SBR BR NBR CR EPDM IIR<br />
Paraffinic + + + - - + +<br />
Naphthenic + + + 0 0 + 0<br />
Aromatic + + + + + 0 -<br />
+<br />
0<br />
-<br />
compatible<br />
partially compatible<br />
incompatible<br />
14
PROCESS OILS<br />
Important Properties of Process Oils<br />
2. Colour stability/Contact staining<br />
Colour stability (increasing darkness) decreases with<br />
increasing % aromaticity.<br />
paraffinic <strong>oils</strong> > naphthenic <strong>oils</strong> > aromatic <strong>oils</strong><br />
3. Ageing resistance<br />
Ageing resistance decrease with increasing % aromaticity.<br />
paraffinic <strong>oils</strong> > naphthenic <strong>oils</strong> > aromatic <strong>oils</strong><br />
15
PROCESS OILS<br />
4. Loss of oil during high temperature service of rubber<br />
product containing oil.<br />
• Determined by FLASH POINT<br />
5. Toxicity<br />
Important Properties of Process Oils<br />
• Become increasingly important<br />
• Process <strong>oils</strong> contain Polycyclic Aromatic Hydrocarbons (PAHs)<br />
or Polycyclic Aromatic (PCA) which are carcinogen and can<br />
cause mutation.<br />
• Regulations (European Directive 2005/69/EC) imposed ban of<br />
<strong>process</strong> <strong>oils</strong> containing ≥ 10mg/kg (ppm) of PAH since<br />
2010.<br />
16
PROCESS OILS<br />
Important Properties of Process Oils<br />
• Trend towards low PAH (
PROCESS OILS<br />
Polycyclic Aromatic Hydrocarbons<br />
PAH S Chemical Formulas MW (g.mol -1 ) Chemical Structures<br />
18
PROCESS OILS<br />
Polycyclic Aromatic Hydrocarbons<br />
PAH S Chemical Formulas MW (g.mol -1 ) Chemical Structures<br />
19
PROCESS OILS<br />
Comparison of Different Process Oils<br />
Effects on properties of rubber compounds and vulcanisates<br />
Process Oils Compared<br />
Aromatic<br />
Naphthenic<br />
Paraffinic<br />
Sample number Saybolt viscosity VGC<br />
1<br />
2<br />
3<br />
4<br />
5<br />
6<br />
7<br />
8<br />
9<br />
10<br />
11<br />
12<br />
13<br />
14<br />
15<br />
38°C 100°C<br />
4360<br />
3500<br />
-<br />
2520<br />
2206<br />
760<br />
156<br />
-<br />
110<br />
104<br />
2642<br />
500<br />
-<br />
110<br />
-<br />
210<br />
96<br />
81<br />
85.9<br />
84.7<br />
60<br />
41.0<br />
43.5<br />
38.2<br />
38.0<br />
155<br />
63.5<br />
42.3<br />
40.4<br />
38.0<br />
0.991<br />
0.954<br />
0.981<br />
0.883<br />
0.882<br />
0.869<br />
0.878<br />
0.830<br />
0.886<br />
0.871<br />
0.800<br />
0.803<br />
0.805<br />
0.807<br />
0.832<br />
20
PROCESS OILS<br />
Comparison of Different Process Oils<br />
FORMULATION FOR OIL EVALUATION<br />
NR<br />
Zinc oxide<br />
Stearic acid<br />
N-330 carbon black<br />
N- Isopropyl-N’ -phenyl-p-phenylenediamine<br />
Oil<br />
N- Oxydiethylenebenzothiazole-2-sulphenamide<br />
Sulphur<br />
Part by weight<br />
100<br />
5<br />
2.5<br />
45<br />
1.5<br />
10 or 20<br />
0.8<br />
2.5<br />
MIX CYCLE : BR BANBURY<br />
Time (min)<br />
0<br />
0.5<br />
1.0<br />
2.0<br />
3.5<br />
Action<br />
Add rubber.<br />
Add small powders.<br />
Add half black.<br />
Half black plus oil.<br />
Dump.<br />
21
PROCESS OILS<br />
Comparison of Different Process Oils<br />
Effects on Mooney Viscosity<br />
Mooney viscosity, ML 1+4, 100 ° C<br />
Mooney viscosity, ML 1+4, 100 ° C<br />
60<br />
50<br />
50<br />
40<br />
30<br />
20<br />
10<br />
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15<br />
Aromatic Oils Naphthenic Oils Paraffinic Oils<br />
10 phr<br />
Naphthenic <strong>oils</strong> tend to give lower<br />
mooney viscosity<br />
40<br />
30<br />
20<br />
10<br />
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15<br />
Aromatic Oils Naphthenic Oils Paraffinic Oils<br />
20 phr<br />
Paraffinic <strong>oils</strong> tend to give lower<br />
mooney viscosity<br />
22
PROCESS OILS<br />
Comparison of Different Process Oils<br />
Vulcanisation Characteristics (ODR 100°C)<br />
Oil Type Sample 10 phr oil 20 phr oil<br />
Aromatic<br />
Naphthenic<br />
Paraffinic<br />
1<br />
2<br />
3<br />
4<br />
5<br />
6<br />
7<br />
8<br />
9<br />
10<br />
11<br />
12<br />
13<br />
14<br />
15<br />
t s5<br />
(min)<br />
4.12<br />
3.42<br />
4.16<br />
3.58<br />
3.53<br />
5.16<br />
3.52<br />
3.47<br />
3.48<br />
4.15<br />
4.07<br />
3.57<br />
4.04<br />
4.00<br />
4.21<br />
T c (90)<br />
(min)<br />
14.33<br />
13.13<br />
13.47<br />
14.31<br />
13.40<br />
14.51<br />
14.43<br />
14.28<br />
14.21<br />
13.56<br />
14.20<br />
14.22<br />
14.45<br />
13.45<br />
14.06<br />
M HR<br />
(torque<br />
33.0<br />
35.6<br />
32.9<br />
32.5<br />
35.5<br />
30.2<br />
33.5<br />
32.1<br />
35.5<br />
32.7<br />
34.6<br />
33.4<br />
33.9<br />
32.5<br />
35.5<br />
M L<br />
units)<br />
7.35<br />
7.45<br />
8.25<br />
7.39<br />
7.36<br />
9.25<br />
7.41<br />
8.16<br />
7.37<br />
7.58<br />
7.44<br />
7.52<br />
7.57<br />
7.13<br />
7.28<br />
t s5<br />
(min)<br />
4.51<br />
3.58<br />
4.25<br />
4.39<br />
4.28<br />
5.00<br />
4.17<br />
4.25<br />
4.17<br />
4.31<br />
4.26<br />
4.35<br />
4.35<br />
4.29<br />
4.39<br />
T c (90)<br />
(min)<br />
16.00<br />
14.32<br />
14.28<br />
15.18<br />
15.11<br />
16.05<br />
14.50<br />
15.24<br />
16.02<br />
15.18<br />
15.13<br />
14.32<br />
16.28<br />
14.58<br />
15.00<br />
M HR<br />
(torque<br />
24.3<br />
27.2<br />
30.3<br />
28.7<br />
27.4<br />
25.4<br />
30.5<br />
27.8<br />
27.2<br />
27.6<br />
28.0<br />
28.8<br />
26.3<br />
27.2<br />
26.4<br />
M L<br />
units)<br />
8.46<br />
7.08<br />
9.00<br />
8.16<br />
8.25<br />
8.53<br />
7.50<br />
8.42<br />
8.22<br />
7.58<br />
8.07<br />
8.16<br />
8.56<br />
8.28<br />
8.14<br />
Little difference was observed for various oil types at 10 and 20 phr. 23
PROCESS OILS<br />
Hardness, IRHD<br />
70<br />
Comparison of Different Process Oils<br />
Effect on Hardness<br />
60<br />
50<br />
40<br />
30<br />
20<br />
Average Values of Hardness for<br />
the Three Oil Types<br />
Dosage<br />
(phr)<br />
A N P<br />
10 62 61.5 62<br />
20 56.5 56 54.5<br />
10<br />
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15<br />
Aromatic Naphthenic Paraffinic<br />
20 phr<br />
Some effects on hardness<br />
• Almost no effect on hardness at<br />
10 phr.<br />
• At 20 phr. paraffinic <strong>oils</strong> show<br />
slightly greater softening effect.<br />
24
PROCESS OILS<br />
Comparison of Different Process Oils<br />
Tensile strength, MPa<br />
Effect on Tensile Strength<br />
30<br />
8<br />
25 2<br />
6 7 9<br />
3<br />
11<br />
10<br />
12 13 14 15<br />
1<br />
4 5<br />
20<br />
unaged<br />
15<br />
10<br />
5<br />
aged 28 days 70 ° C<br />
aged 3 days 100 ° C<br />
Aromatic Naphthenic Paraffinic<br />
20 phr of oil<br />
aged 7 days 100 ° C<br />
• Individual <strong>oils</strong> gave widely different values of T.S<br />
• Effect of different types of <strong>oils</strong> on unaged, 70 ° C aged or<br />
100 ° C aged are slight. 25
PROCESS OILS<br />
Comparison of Different Process Oils<br />
Compression set, %<br />
60<br />
Effect on Compression Set<br />
50<br />
1 day 100 ° C<br />
40<br />
30<br />
7 days 70 ° C<br />
20<br />
10<br />
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15<br />
Aromatic Naphthenic Paraffinic<br />
20 phr of oil/25% initial compression<br />
Paraffinic and naphthenic <strong>oils</strong> tend to give lower<br />
compression set values than aromatic oil. 26
PROCESS OILS<br />
Comparison of Different Process Oils<br />
Effect on Dunlop Resilience<br />
Dunlop resilience, 23 ° C, %<br />
80<br />
70<br />
60<br />
50<br />
40<br />
30<br />
20<br />
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15<br />
Aromatic Naphthenic Paraffinic<br />
20 phr of oil<br />
• Aromatic oil gave lower resilience<br />
• Higher viscosity <strong>oils</strong> gave lower resilience<br />
27
PROCESS OILS<br />
Performance of Low PAH/PCA Oils<br />
Rolling Resistance<br />
110<br />
108<br />
106<br />
104<br />
102<br />
Wet Grip<br />
+<br />
TDAE<br />
MES<br />
NAP<br />
RAE<br />
100<br />
98<br />
96<br />
94<br />
92<br />
90<br />
DAE TDAE MES NAP RAE<br />
-<br />
-<br />
Rolling Resistance<br />
+<br />
28
PROCESS OILS<br />
SUMMARY<br />
1. Process <strong>oils</strong> are used to improve the <strong>process</strong>ability of rubber<br />
compounds or to increase the bulk of rubber in order to lower cost.<br />
2. Although <strong>process</strong> <strong>oils</strong> are classified as paraffinic (CP) naphthenic<br />
(CN) or aromatic (CA), they are mixtures of CP/CN/CA.<br />
3. The efficiency of oil in reducing viscosity and elasticity depends on<br />
its compatibility with rubber or its solubility in rubber.<br />
- good compatibility/solubility efficient<br />
- smaller quantity may be used.<br />
4. Compatibility or efficiency depends on<br />
- % aromaticity : the higher, the more efficient<br />
- MW or viscosity : the smaller, the more efficient<br />
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PROCESS OILS<br />
SUMMARY<br />
5. Study on NR compounds showed that the vulcanisation properties<br />
and vulcanisate properties, unaged and aged, are not greatly<br />
affected by type of <strong>process</strong> oil.<br />
6. Toxicity of <strong>process</strong> <strong>oils</strong> is of major concern at present.<br />
- Polycyclic Aromatic Hydrocarbon (PAH) is carcinogen and<br />
may cause mutation.<br />
7. European Directive 2005/69/EC imposed ban on <strong>process</strong> <strong>oils</strong><br />
containing ≥10 ppm of PAH since 2010.<br />
8. The developing trend in <strong>process</strong> oil is towards low PAH <strong>oils</strong>.<br />
- TDAE<br />
- MES<br />
- NAP<br />
- RAE<br />
- Vegetable <strong>oils</strong> 30
Q & A<br />
31