Four different GAP mixtures with di‐ and tri‐functional GAP types were successfully cured with bis‐propargyl‐succinate (BPS) via 1,3 dipolar cycloaddition reaction between the azido groups of GAP and the triple bonds of the propargyl ester. Investigation of one series of curing on di‐functional and another series on tri‐functional GAP was done and compared with two additional curing series on mixtures of di‐ and tri‐functional GAP. The BPS which acted as a curing agent analog to isocyanate in classical polyurethane systems, was varied in its content, and the influence on the mechanical properties of the cross‐linked binders was measured by tensile tests. The mechanical properties could be adjusted in a wide range by varying the amount of BPS. The E modulus of the tested samples was in the range of 0.06–0.674 N mm−2 at elongations between 50 and 95% and the maximum stress was in the range of 0.05–0.32 N mm−2. Increasing contents of BPS showed, in thermal analysis by DSC, only a small decrease in the decomposition energy and slightly raised glass transition temperatures. The required amount of inert curing agent for complete cure of GAP is lower for BPS in comparison to isocyanate, so this will result in a higher total energy content in the binder system. However, BPS‐cured systems can lead to higher glass transition temperatures than isocyanate‐based binder systems. The curing process has been monitored by measuring the increasing viscosity at 50 and 60 °C. The curing time of the investigated binder systems for quantitative curing at 65 °C is around four days, which was checked by measuring the surface hardness, but at room temperature the premixed curing samples staid liquid for around 1 week.

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The occurrence and shape of turbulent structures in mixed convection flows through a differently heated vertical channel are investigated in terms of thermally induced attenuation and amplification of turbulent velocity, pressure, and temperature fluctuations using direct numerical simulations. It is shown that the wall‐normal momentum transport is decreased and increased near the heated and cooled wall, respectively, and that this leads to a reduced and elevated production of turbulent velocity fluctuations in the streamwise velocity component in the aiding and opposing flow, respectively. The corresponding flow structures are smoother, faster and warmer in the aiding flow and aligned along the main flow, while the colder structures in the opposing flow are more frayed and less directed. The warmer flow structures in the aiding flow are overall more stable than the colder structures in the opposing flow. Besides, the study reveals that the position of the maximum temperature fluctuations moves toward the heated wall, so that the sweeps produced at the two walls are affected differently by the former. As a consequence, the distance and time period over which the fluctuations develop in the aiding flow are shorter than in the opposing flow. It is further shown that vortex structures oriented in the streamwise direction usually arise with an offset to the right or left above a sweep or an ejection, whereby the decreasing values of the correlation coefficients with increasing Grashof number indicate a weakening of the vortex structures. Since none of the evaluated vortex criteria, that is, the distributions of the vorticity, λ2‐ value or Rortex‐value correlate well with the evaluated minima of the pressure fluctuations, they do not allow a clear identification of the vortex structures. Finally, analyzing the budget of the turbulent kinetic energy it is confirmed that the velocity fluctuations are only indirectly influenced by the buoyancy force. Thus, the attenuation and amplification of the turbulent velocity fluctuations is reflected in the reduction and exaggeration of the Reynolds shear stresses in the aiding and opposing flow, respectively.

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