The Vulcanization of Elastomers. X. The Vulcanization of Natural Rubber with Thiuram Disulfides (V)

1957 ◽  
Vol 30 (3) ◽  
pp. 903-910
Author(s):  
Otto Lorenz ◽  
Walter Scheele ◽  
Wolfgang Redetzky

Abstract The kinetics of crosslinking natural rubber during vulcanization with tetramethyl and tetraethylthiuram disulfide was investigated. The following results were derived: 1. The increase of crosslinking during vulcanization which was measured by the change of reciprocal swelling is first order over a wide range of reaction time and temperature. 2. During vulcanization, crosslinking and dithiocarbamate formation are reactions which proceed with identical rate. From this we had to conclude that the formation of dithiocarbamate is the immediate cause of the crosslink formation. 3. The concentration of the thiuram disulfide decreases much faster with respect to vulcanization time than crosslinking increases. In other words, the thiuram decrease can only be considered a reaction which precedes crosslinking.

1957 ◽  
Vol 30 (1) ◽  
pp. 77-86 ◽  
Author(s):  
Walter Scheele ◽  
Horst-Eckart Toussaint

Abstract The vulcanization of Buna S-3 by tetraethylthiuram disulfide is reported. A quantitative study of the transformation reactions led to the following results. (1) Using tetraethylthiuram disulfide as representative of the class, it was found that two thirds of it undergoes transformation to zinc dithiocarbamate during the vulcanization of Buna S-3, independent of the temperature. (2) Both the decrease of thiuram disulfide and increase of dithiocarbamate are first-order reactions within a wide range of the transformation. (3) The rate constants of the decrease of thiuram and of the increase of dithiocarbamate are a little less than a tenth power greater than for the vulcanization of natural rubber. This is possibly explainable by the different structure of the allyl units in Buna S-3. (4) The activation energies of the decrease of thiuram as well as the increase of dithiocarbamate are nearly the same and are greater than for the vulcanization of natural rubber.


The first, second and third explosion limits for the hydrogen/oxygen reaction have been examined over a wide range of temperature, mixture composition, vessel size and wall coating. An expression has been derived from general chain theory which can account for the observed features of the complete explosion region. It includes and relates previously given expressions for the individual limits. The reactions found to be necessary and apparently sufficient to account for the hydrogen/oxygen spontaneous ignition peninsula are those of chain destruction in triple collisions, destruction at the wall of three different chain carriers, first-order branching, second-order branching, the regeneration of ‘dead’ chains and a chain-initiating process.


2012 ◽  
Vol 9 (1) ◽  
pp. 203-210 ◽  
Author(s):  
Mahantesh A. Angadi ◽  
Suresh M. Tuwar

t-Butylbenzylamine (t-BA) is used as a free base in the synthesis of salbutamol drug. Its mechanism of oxidation was proposed from kinetic studies. The kinetics of oxidation oft-butylbenzylamine by diperiodatoargentate(III) (DPA) was studied spectrophotometrically by monitoring decrease in absorbance of DPA. The reaction was found to be first order each in [DPA] and [t-BA]. The effect of alkali concentration in a wide range on rate of reaction was studied. The rate of reaction was found to be increased with increase in [OH–] in the lower range of [OH–], decreasing effect in the middle range and at higher range again increasing effect on rate of reaction was observed. The added periodate retarded the rate of reaction. The polymerization test revealed that oxidation was occurred with the intervention free radical. A suitable mechanism was proposed for a middle range of [OH–]. The active species of silver(III) periodate for all the three different stages of [OH–] are assayed. Rate law was derived and verified. The oxidative product oft-BA was characterized by LC-ESI-MS spectra.


2019 ◽  
Vol 80 (12) ◽  
pp. 2250-2259
Author(s):  
Xiaoyu Deng ◽  
Dachao Zhang ◽  
Meng Wu ◽  
Philip Antwi ◽  
Hao Su ◽  
...  

Abstract Aerofloats, such as aniline aerofloat ((C6H5NH)2PSSH), are extensively employed for collection activities in wastewater particularly in cases where minerals are in flotation. Although this aniline aerofloat has efficient collection properties, they are ordinarily biologically persistent chemicals in which case their residual, as well as their byproducts, pose great environmental risks to water and soils. In this study, the removal efficiency of aniline aerofloat (AAF) by a combined vacuum ultraviolet (VUV) and ozone (O3) process (VUV/O3) was evaluated. Furthermore, the impacts of pH, O3, the concentration of AAF and coexisting ions (SiO32−, CO32−, Cl− (Na+), SO42−, Ca2+) were systematically studied. The experiments revealed that, with an initial AAF of 15 mg/L, AAF removal >88% was feasible with a reaction time of 60 min, pH of 8 and O3 of 6 g/h. The order of influence of the selected coexisting ions on the degradation of AAF by VUV/O3 was Ca2+ > CO32− > SiO32− > Cl− (Na+) >SO42−. Compared with VUV and O3 in terms of pollutant degradation rate, VUV/O3 showed a remarkable performance, followed by O3 and VUV. Additionally, the degradation kinetics of AAF by the VUV/O3 process agreed well with first-order elimination kinetics.


2013 ◽  
Vol 86 (4) ◽  
pp. 604-614 ◽  
Author(s):  
Lanzhen He ◽  
Jieping Zhong ◽  
Jing Chen ◽  
Chenpen Li ◽  
Linxue Kong ◽  
...  

ABSTRACT The kinetics of the chlorination of low-concentration natural rubber latex was investigated. The kinetic data were derived from chlorine concentrations in chlorinated natural rubber (CNR) for different reaction times and temperatures. The chlorination reaction process can be divided into two stages—a high-speed period (stage 1) and a low-speed period (stage 2)—using the graphed curves of the change in chlorine content with change in reaction time. The relationship of the chlorination conversion ratio x to reaction time t and temperature T can be expressed as x = 1.15 − 0.916e−kt, where the kinetic constant k = 0.00907 + 6.39 × 10−6e0.0211T. The overall apparent reaction order n for the first stage is 4.8, whereas for the second stage it is 1.0, using kinetic fitting. The apparent activation energy Ea was calculated, using the Arrhenius equation, to be 5.32 kJ/mol for stage 2. The lower value of Ea suggests that the chlorination rate is less sensitive to reaction temperature in this stage. The chlorination reaction rate increases with the increase in reaction temperature during stage 2, but the effects are not visible. However, a temperature that is too high may result in energy being wasted. We conclude that the proper reaction temperature in stage 2, taking the kinetic effects into account, is between 323.15 and 353.15 K.


1964 ◽  
Vol 37 (4) ◽  
pp. 910-926 ◽  
Author(s):  
W. Scheele ◽  
H. Müller ◽  
W. Schulze

Abstract In continuation of earlier work with natural rubber, the kinetics of sulfur decrease were studied in certain synthetic rubbers for different temperatures and sulfur concentrations. At the same time the formation of polysulfide bound sulfur was studied, using as example the reaction of sulfur with natural rubber and synthetic rubbers. It was found that: 1) When the decrease in sulfur concentration is portrayed by curves which are convex to the time axis (Perbunan), the 0.6th order time-law is fulfilled, (as in the case of natural rubber independent of temperature and concentration. 2) In contrast, the concentration dependence of the rate at which sulfur decreases, both in Perbunan and cis 1,4-polybutadiene, denotes a first-order reaction in agreement with experience with natural rubber. 3) The activation energy of sulfur decrease has the same magnitude for all the elastomers investigated (34 to 36 kcal/mole). 4) The disagreement between the time law and the concentration dependence of the rate of sulfur disappearance encountered in all the experiments with 1,5-polyenes, is interpreted as indicating autocatalysis, which likewise explains the shape of the curves for sulfur disappearance. 5) Sulfur reacts considerably faster in natural rubber and Perbunan than in cis 1,4-polybutadiene; consequently a homolytic dissociation of the S8-ring cannot be rate-determining. 6) Polysulfide sulfur shows, in each case, a maximum with reaction time, and in completely reacted vulcanizates it tends toward a limiting value. An equation was found, which provides a good description of change with time of polysulfide concentration (natural rubber and cis 1,4-polybutadiene). 7) An explanation is given for the appearance of the polysulfide maximum; and how the reaction of sulfur with 1,5-polyenes can be represented, making use of all available results, is discussed.


2020 ◽  
Vol 9 (1) ◽  
pp. 1-11
Author(s):  
Agus Haryanto ◽  
Amieria Citra Gita ◽  
Tri Wahyu Saputra ◽  
Mareli Telaumbanua

This research aims to study the first-order kinetics of biodiesel production from used frying oil (UFO) through transesterification with methanol. Used frying oil was collected from fried peddlers around the campus of the University of Lampung. Technical grade methanol and NaOH catalyst were purchased from a local chemical supplier. The experiment was carried out with 100 ml of UFO at various combinations of oil to methanol molar ratio (1:4, 1:5, and 1:6), reaction temperatures(30 to 55oC, the ramping temperature of 5o C), and reaction time of 0.25 to 10 minutes. First-order kinetic was employed using 126 data pairs (87.5%). The acquired kinetic model was validated using 18 data sets (12.5%) observed at a reaction time of eight min. Results show that biodiesel yield was increased with reaction time, its molar ratio, and temperature. The maximum return of 78.44% was achieved at 55oC and molar ratio of 1:6. The kinetic analysis obtains the reaction rate constant (k) in the range of 0.045 to 0.130. The value of k increases with the reaction temperature and molar ratio. The analysis also reveals the average activation energy (Ea) of the UFO transesterification reaction with methanol and NaOH catalyst to be 21.59 kJ/mol. First-order kinetic is suitable to predict biodiesel yield from UFO because of low %RMSE (3.39%) and high R2 (0.8454


1956 ◽  
Vol 29 (1) ◽  
pp. 37-48 ◽  
Author(s):  
Walter Scheele ◽  
Otto Lorenz

Abstract If we disregard for the moment the phenomena which occur in the interaction of thiuram disulfide with geraniol under the influence of air and confine our consideration to the results which can be deduced from the study of this reaction in a stream of nitrogen, we are led to the conclusion that geraniol, which was used as a model compound, behaves with respect to its interaction with tetraethylthiuram disulfide, not only qualitatively but also quantitatively, exactly like rubber, and that it is not to be assumed that other tetraalkylthiuram disulfides as well as other compounds which are analogous to geraniol will behave differently. Thus the results can be evaluated as a proof that the vulcanization of natural rubber by thiuram disulfides depends on nothing other than a definite and always similar interaction with the allyl groups of the polyisoprene chain. The results of the investigation described in this paper can be regarded, moreover, as support for the correctness of our procedure in the clarification of the vulcanization mechanisms, and they stress the importance of analytical-chemical methods, which have certainly not been pursued in the past with the necessary intensity and insight. These investigations are being continued. It has already been found that the vulcanization of natural rubber with thiuram monosulfides and sulfur leads to the same results as vulcanization with thiuram disulfides. This has been conjectured, to be sure, by a number of workers. However, it was never really demonstrated experimentally. We shall report on this in the near future. The experimental results can now be summarized as follows : 1. The reaction between thiuram disulfide and geraniol (demonstrated by the example of tetraethylthiuram disulfide) takes place qualitatively and quantitatively like the interaction between thiuram disulfide and natural rubber. In the vulcanization of rubber by thiuram disulfides, therefore, there is involved a reaction of the thiuram disulfide with the allyl groups, leading to a definite conversion. 2. It was found that in the interaction of geraniol with thiuram disulfide under nitrogen and in the presence of zinc oxide, the limiting value of zinc dithiocarbamate amounts to 66 mole-per cent of the original thiuram disulfide, independent of the temperature. This was the result found in the study of the reaction of the thiuram disulfides with rubber. 3. We were able to show that the limiting value of the dithiocarbamate yield in the interaction of tetraethylthiuram disulfide with geraniol is independent of the thiuram disulfide concentration. This is likewise true for the reaction of the thiuram disulfides with natural rubber. From this it follows that the interaction of thiuram disulfides with allyl groupings, as they occur in the polyisoprene chain, is apparently a stoichiometric one. For this reason we can no longer retain the assumption that the limiting value of the yield of dithiocarbamate is the result of a sterically hindered reaction. 4. The change of concentration of zinc dithiocarbamate in the interaction of tetraethylthiuram disulfide with geraniol under nitrogen can be accounted for by postulating a reaction of the first order. The velocity constants were calculated and it was found that the resulting activation energy is somewhat greater than the one for the interaction with natural rubber. 5. Similarly the concentration of thiuram disulfide obeys a first-order reaction as it falls off to zero. The velocity constants were calculated. The activation energy obtained from the temperature dependence is in good agreement with that found for the interaction with rubber. 6. In the presence of oxygen, the reaction between thiuram disulfide and geraniol takes a quite different course. The rate of decrease of concentration of thiuram disulfide, which likewise follows a first-order reaction, is higher. The yield of zinc dithiocarbamate does not attain the constant value of 66 mole-per cent of the original thiuram disulfide. In the temperature range studied, the amount of dithiocarbamate found is smaller. The limiting value reached at the various temperatures is progressively smaller, the lower the temperature chosen. Whether by expanding the temperature range, one would eventually reach a minimum and a maximum limiting value has not been investigated.


2019 ◽  
Vol 29 (1) ◽  
pp. 162-172
Author(s):  
Peng Wang ◽  
Dietmar Auhl ◽  
Eckart Uhlmann ◽  
Georg Gerlitzky ◽  
Manfred H. Wagner

Abstract Polyurethane (PU) elastomers with their broad range of strength and elasticity are ideal materials for additive manufacturing of shapes with gradients of mechanical properties. By adjusting the mixing ratio of different polyurethane reactants during 3D-printing it is possible to change the mechanical properties. However, to guarantee intra- and inter-layer adhesion, it is essential to know the reaction kinetics of the polyurethane reaction, and to be able to influence the reaction speed in a wide range. In this study, the effect of adding three different catalysts and two inhibitors to the reaction of polyurethane elastomers were studied by comparing the time of crossover points between storage and loss modulus G′ and G′′ from time sweep tests of small amplitude oscillatory shear at 30°C. The time of crossover points is reduced with the increasing amount of catalysts, but only the reaction time with one inhibitor is significantly delayed. The reaction time of 90% NCO group conversion calculated from the FTIR-spectrum also demonstrates the kinetics of samples with different catalysts. In addition, the relation between the conversion as determined from FTIR spectroscopy and the mechanical properties of the materials was established. Based on these results, it is possible to select optimized catalysts and inhibitors for polyurethane 3D-printing of materials with gradients of mechanical properties.


1966 ◽  
Vol 39 (3) ◽  
pp. 768-784 ◽  
Author(s):  
Walter Scheele ◽  
Ernst Rohde

Abstract The present article reports experiments intended to elucidate the kinetics of benzoyl peroxide decompositions in natural rubber and polybutadiene, and of consequent reactions. Both in natural rubber and in polybutadiene and at all temperatures, peroxide decomposition is first order with respect to concentration as well as time. The decomposition rate is substantially higher in natural rubber than in polybutadiene, and independent of the constitution of the polymer chains of the polybutadiene (tacticity, vinyl side groups, and the like). A somewhat higher activation energy of peroxide decomposition was derived for polybutadiene than for natural rubber. Formation of benzoic acid and crosslinking both follow a first order time law; the rates for peroxide decomposition, formation of benzoic acid, and crosslinking are the same in natural rubber and polybutadiene. It seems probable that peroxide decomposition in polybutadiene is purely homolytic. Interaction between peroxide and natural rubber is assumed, resulting in an increase in the rate of decomposition. The benzoic acid yield is considerably higher in natural rubber than in polybutadiene, and diminishes in the latter with the increase in vinyl side groups. In natural rubber this yield is a function of temperature, but in polybutadiene it shows practically no temperature dependence. Benzoyloxy radicals are incorporated into the elastomers as benzoate groups, as confirmed by infrared spectroscopic determinations with cis-1,4 polybutadiene. An interpretation of the formal kinetics of the vulcanization of 1,5-polyenes is proposed, which, together with the experimental results, may be used as a basis for consideration of the reaction mechanism.


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