Understanding “the difference between the structure and processing of thermoplastics and thermocondensed plastics” requires that the physical flow of material structures, heat history and equipment be placed on the same chain of causality. The key mechanisms for this theme are thermal softening and remelting of thermoplastic resins and the formation of a conjunctive network of thermal solidified systems, which have very different plasticization equipment and temperature control logic. The material structure, thermal performance and flow base determine the path to plasticization and cannot simply reproduce temperature and velocity by trade name. Therefore, the name of the material and the recommended setting can only be used as a starting point, and the actual judgement is to return to the plate number, water, filling and assistor, the single total quantity, cycle, screw structure and product requirements to confirm whether the temperature, cut and stay of the material in the equipment is safe.

At the test-model or volume-import phase, a list of inputs should be established around “the differences in the structure and processing of thermoplastics and thermosolids”, including feedstock suppliers and batches, technical data sheets, drying conditions, the ratio of colored mothers and respirators, specifications of equipment to screws, product and fluid weights, the temperature of the moulds and existing defects. It is recommended that first the batch of materials be fixed, the oven state and the mold cooling, and then that the cooling of the drums be recorded, the timing of measurements, the screw twist, the back pressure and the injection peak pressure. The main risk of the subject is that heat-condensing of thermal solid materials over long periods of time to heat thermal plastics will jam the flowways ahead of time, while thermal plastics have unmelted and high rectangles. Parameters must be recorded in a specific pattern to distinguish material from equipment from operational changes.

Control methods should not begin with blindly increasing temperature or pressure, but should be based on "substance state - feed drying" The sequence of screw plasticization - nozzles and fluids - product results. Parameter optimization should give priority to ensuring that materials are free of hydrolysis, overheating and unsmelting, and then discuss speed, pressure and cycle; otherwise, the appearance of satisfactory may be at the expense of long-term performance. The site adjusts only one main variable at a time, while observing the actual melting temperature, measuring time, screw twists, mats, injection pressure, product weight, colour, scent and critical dimensions. If production can only be sustained by extreme parameters, the use of a switch to cover the material or hardware boundary should be discontinued.

The verification of “conformities between the structures and processes of thermoplastics and thermosolids” suggests a repetitious approach: checking resin types, solidification mechanisms, recommending temperature, reversibility and machine clean-up methods, and identifying them through twists and product appearances. A baseline should be established after the first eligibility and the water-bearing rate, melting temperature, measuring curves and critical energy should be measured by production tonnage. The technical agreement between the supplier and the plant shall state the material, the sampling method, the detection project, the permitted scope and the change notification requirements. The plasticization programme can only be considered to have long-term quantitative value if the product ' s probabilities, performance, cyclicality, energy consumption and maintenance costs are met in a continuous production process.