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Compensating extra sulfur to TESPD-silica-filled NR

compounds

Wisut Kaewsakul*, Kannika Sahakaro, Wilma K. Dierkes, Jacques Noordermeer and Anke Blume

Elastomer Technology and Engineering (ETE), Department of Mechanics of Solids, Surfaces and Systems (MS3), University of Twente, The Netherlands

Background

Experimental

Results

Conclusions

TESPT can liberate free sulfur into the

system, resulting in an undesired high

compound viscosity caused by ‘premature

scorch’ [1].

 An alternative silane: TESPD, has been

made available.

[1] W. Kaewsakul, K. Sahakaro, W.K. Dierkes and J.W.M. Noordermeer, Rubber Chemistry and Technology 2012, 85 (2), 277-294. [2] W. Kaewsakul, K. Sahakaro, W.K. Dierkes and J.W.M. Noordermeer, Rubber Chemistry and Technology 2013, 86 (2), 313-329. [3] W. Kaewsakul, K. Sahakaro, W.K. Dierkes and J.W.M. Noordermeer, Kautschuk Gummi Kunststoffe 2014, 67 (5), 33-39.

The addition of extra sulfur in an internal mixer during non-productive step gives a

positive contribution towards improved silica dispersion, and hence final properties.

Adding extra sulfur during productive mixing on a two-roll mill has practically no effect.

 Extra sulfur at 3.4-5.1 wt% relative to the TESPD amount (0.15-0.20 phr), added during

mixing of TESPD-silica-NR in an internal mixer is an optimal amount.

Compound viscosity and cure properties

 An internal mixer with fill factor of 70 %,

a rotor speed of 60 rpm, starting

temperature of 100oC to reach 140-145oC.

*Correspondence: W. Kaewsakul, PhD, assistant professor; e-mail: w.kaewsakul@utwente.nl

0 20 40 60 80 100 120 140 0 2 4 6 8 10 12 14 16 18

Extra sulfur (wt% rel. to TESPD)

ML (1 + 4 )100 o C Two-roll mill Internal mixer TESPT 0 10 20 30 40 50 60 70 80 0 2 4 6 8 10 12 14 16 18

Extra sulfur (wt% rel. to TESPD)

B ound r ubbe r c ont e nt ( % ) TESPT Chemically BdR Total BdR Physically BdR Without extra sulfur

0.000 0.001 0.002 0.003 0.004 0.005 0.006 20 30 40 50 60 70 80 90 Chemically BdR content (%) Flocc ulation ra te c ons tant , k a ( s -1 ) 0 10 20 30 40 50 60 70 80 90 100 110 120 ML (1 + 4 )1 00 o C ka_TESPT ML(1+4)_TESPT increase in extra sulfur increase in extra sulfur 0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 20 30 40 50 60 70 80 90 Chemically BdR content (% ) [G '( 0 .56 )-G '( 100 )] , G ' (M P a ) 0 1 2 3 4 5 6 7 8 9 R ei n fo rcem en t p a ram et er , α F _TESPT _TESPT increase in extra sulfur increase in extra sulfur ΔG' (TRM) αF (TRM) ΔG' (IM) αF (IM) αF ΔG' ∆ 0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0 0 2 4 6 8 10 12 14 16 18

Extra sulfur (wt% rel. to TESPD)

Reinforce ment inde x , M 3 00 /M 1 00 Two-roll mill Internal mixer TESPT 0 5 10 15 20 25 30 35 0 2 4 6 8 10 12 14 16 18

Extra sulfur (wt% rel. to TESPD)

Te ns ile s tr e ngt h ( M P a ) 0 100 200 300 400 500 600 700 800 900 1000 E longa tion a t br e a k ( % ) Two-roll mill Internal mixer TESPT

Mechanical properties of vulcanizates

Indicators of filler-rubber interactions and lightly crosslinked rubber networks.

References:

TESPT – the most commonly used silane coupling agent

Chemical name: Bis-triethoxysilylpropyl tetrasulfide (-S4-)

TESPD – An alternative to TESPT, preventing a scorch problem

Chemical name: Bis-triethoxysilylpropyl disulfide (-S2-)

Extra networks can suppress the mobility of

silica clusters but give undesired high viscosity at a certain content of extra sulfur added.

Adding extra sulfur during non-productive mixing gives a significant impact on filler-filler interaction or

Payne effect & reinforcement.

S4 (CH2)3 (CH2)3 Si Si OC2H5 OC2H5 OC2H5 H5C2O H5C2O H5C2O S2 (CH2)3 (CH2)3 Si Si OC2H5 OC2H5 OC2H5 H5C2O H5C2O H5C2O

According to the previous study [2], the TESPT-based compounds showed

superior overall properties compared to those containing TESPD, mainly

attributed to the influence of free sulfur liberated.

 The present study investigates an effect of extra sulfur added to silica-filled NR

compounds during non- and productive mixing processes [3].

Remark: The results presented in this poster have been published in Kautschuk Gummi Kunststoffe 2014, 67 (5), 33-39 or the reference [3].

 Mixing sequence: NR for 2 min, ½ silica+silane (+ ½ extra sulfur)

for 5 min, ½ silica+silane+TDAE oil (+ ½ extra sulfur) for 5 min,

ZnO+stearic acid+TMQ+ ½ DPG for 3 min, and discharged.

 Sulfur (+extra sulfur)+accelerators+ ½ DPG were added on two-roll mill.

 The measurement methods are described in [3].

0 1 2 3 4 5 6 7 8 9 0 2 4 6 8 10 12 14 16 18

Extra sulfur (wt% rel. to TESPD)

S c or c h & opt im um c ur e t im e s ( m ins .) t10 (IM) tc,90 (TRM) tc,90 (IM) TESPT t10 (TRM) Two-roll mill Internal mixer Note: TRM = Two-roll mill IM = Internal mixer Note: TRM = Two-roll mill IM = Internal mixer Note:

The compounds with extra sulfur added in an internal mixer.

Note:

The compounds with extra sulfur added in an internal mixer.

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