Biodegradable, programmable synthetic polymeric material and its preparation process

A process for manufacturing a biodegradable synthetic polymeric material, comprising the steps of:

• a. binding a first degrading substance from a storage tank through a pipe to a mechanic irrigation system, wherein the first degrading substance comprises betaine (C5H11NO2), cassava (yucca) starch (C6H10O5), carrot carotene (C40H56), water, carbon monoxide, corn glucose (C6H12O6), and a 1 to 6 carbon atoms carboxylic acid;
• b. pelletizing the substance obtained in step a) along with a second degrading substance comprising betaine (C5H11NO2), cassava (yucca) starch (C6H10O5), water, and corn glucose (C6H12O6), and
• c. extruding the mixture of the substance obtained in steps a) and b) through a mechanic sprinkler system, and
• d. sealing the final material obtained;
• wherein the biodegradable synthetic polymer material comprises
• betaine (C5H11NO2) is between 15 and 25% (w/w) in relation to the weight of the total degrading substance;
• the cassava (yucca) starch (C6H10O5) is between 10 and 17% in relation to the weight of the total degrading substance;
• the carrot carotene (C40H56) is between 10 and 15% in relation to the weight of the total degrading substance;
• the water is between 35 and 48% in relation to the weight of the total degrading substance;
• the carbon monoxide is between 0.001% and 10% in relation to the weight of the total degrading substance;
• the corn glucose (C6H12O6) is between 4 and 9%;
• and
• the carboxylic acid is selected from the group consisting of formic acid, propanoic acid, acetic acid and mixtures thereof;
• and
• wherein in step a) the binding container has a mechanic irrigation system where the degrading substance from step a) coming from a storage tank is evenly applied under pressure and in step b) the substance obtained from step b) is in constant recirculation between an upper tank and the receiving tray of the polymeric material through an auxiliary tank with a pumping centrifugal mechanic system and in step c), the mixture of first and second degrading substances from steps a)+b) is applied by a specific homogeneous spraying mechanic system wherein the first and second substances from steps a)+b) is subjected to a pressure between 120 and 220 psi (0.83 MPa to 1.52 MPa), and ejects the substance over the surface of the extruded polymeric film by molding.