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The catalyst support was produced from biopolymers; chitosan and cellulose.
Mayenite support was produced by mixing stoichiometric amounts of calcium hydroxide and aluminium nitrate.
The 5 wt % Ce/γ-Al2O3 support was produced by dissolving cerium III) 2,4-pentanedionate (0.509 g) in toluene, to which γ-Al2O3 (1.805 g) was added.
Subsequently, the resultant mixture was calcined for 6 h at 673 K in 5 % O2/He, and then reduced for 5 h under flowing 5%% H2/He at 573 K. Ceriated Rh/γ-Al 2O 3 (method I): 5 wt % Ce/γ-Al2O3 support was produced by dissolving cerium III 2,4-pentanedionate (0.509 g) in toluene and γ-Al2O3 (1.805 g) was then added.
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The PET microfibers used as a support were produced via electrospinning of viscous PET solution.
The DNA monomers were obtained from Proligo (Sigma-Aldrich) and the LNA monomers and solid support were produced by Santaris Pharma (commercially available from Exiqon, Denmark).
Supported lipid membranes, which adapt to the topography of the underlying PDMS support, were produced using a vesicle fusion technique.
Green planar circular supports were produced and sintered in vacuum at different temperatures.
The "green" metal supports were produced by commercial powder metallurgy methods such as tape casting and high-pressure injection moulding.
The metal supports were produced by the following injection setting parameters: moulding temperature: 120 °C, mould temperature: 40 °C and moulding pressure: 1700 bar.
For this, a loading system was provided to maintain the vertical direction of the load applied to the beam, and a support frame was produced to satisfy the in-plane and out-of-plane support conditions.
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