Low-energy-consumption device for producing expanded polystyrene by bulk process
A technology of expanded polystyrene and low energy consumption, applied in chemical/physical/physicochemical fixed reactors, etc., can solve the problems of high energy consumption, many organic and inorganic pollutants, and high labor intensity of batch polymerization process. To achieve the effect of safe and controllable production process, low risk and good environmental protection effect
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Embodiment 1
[0024] figure 1 It is the process flow diagram that this patent implements, and this specific embodiment adopts the following technical solutions:
[0025] The device of this embodiment includes a polymerization reactor (1), a condenser (3), a pump (4), a mixer (5), a plug flow reactor (6), a static mixer (7), and a plug flow reactor (8), the pump (9), the high-pressure underwater pelletizing system (10), the components are connected in sequence with pipes;
[0026] The upper head of the polymerization reaction unit (1) is provided with a material inlet, a reaction stirrer (2) is installed, a condenser (3) is connected, and the lower end is connected with a discharge pump (4).
[0027] When using the above device to produce expanded polystyrene, the material includes the following components by weight:
[0028] 92.5 kg of styrene and 1.5 kg of low molecular weight polyethylene as auxiliary materials were added to the polymerization reactor (1), and the temperature of the mat...
Embodiment 2
[0035] In this embodiment, on the basis of Embodiment 1, a fifth fluid port is added at the inlet of the front end of the static mixer (7). The fifth fluid is flame retardant polystyrene masterbatch, which contains 0.7kg of flame retardant. The fifth fluid flame retardant polystyrene masterbatch is extruded and input into the static mixer (7) at the front inlet of the static mixer (7) with the third fluid polystyrene, and the fourth fluid blowing agent n-pentane and isopentane. Each 3.0kg is fed into the static mixer (7), sheared and mixed evenly, and then enters the plug flow reactor (8), and then is transported by the pump (9) to the high-pressure underwater pelletizing system (10), and is granulated and dried to obtain resistance. Combustible expandable polystyrene pellets. After testing, the oxygen index of flame-retardant expandable polystyrene reaches 32, which meets the requirements of B1-level fire-resistant materials. The data of EPS prepared by this method and the ...
Embodiment 3
[0042] In this embodiment, on the basis of Embodiment 1, a fifth fluid port is added at the inlet of the front end of the static mixer (7). The fifth fluid is a polystyrene masterbatch containing graphite and flame retardant, which contains 2.0 kg of graphite and 0.3 kg of flame retardant. The fifth fluid graphite polystyrene masterbatch is extruded and input into the static mixer (7) at the front inlet, and the third fluid polystyrene and the fourth fluid blowing agent are merged into the static mixer (7) for shearing. After cutting and mixing evenly, it enters the plug flow reactor (8), and is then input into the high-pressure underwater pelletizing system (10) by the pump (9) for granulation and drying into finished graphite-type expanded polystyrene particles. After testing, the oxygen index of flame-retardant expandable polystyrene reaches 32, which meets the requirements of B1-level fire-resistant materials. The comparative analysis of the data of EPS prepared by this m...
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