Porous carbon-containing compounds as water carriers and cell size controlling agents for polymeric foams
一种聚合物、泡沫板的技术,应用在挤出泡沫产品领域,能够解决增大生产成本、增大停工期等问题,达到增加生产成本的效果
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Embodiment 1
[0087] Composition of 75 wt% polystyrene (NOVA1600 from NOVA Chemical, PA) and 25 wt% powdered activated carbon (DARCO KB-G from Norit Americas, Texas) was prepared by extrusion process using an LMP twin extruder from Leistitz. Microporous compound (PS / PAC25).
[0088] The porosity, pore size and density of the formed microporous compound PS / PAC25 were measured by mercury intrusion analysis. The results are listed in Table 1.
[0089] Table 1 Porosity analysis of microporous PS / PAC25 compound
[0090] project
[0091] Average pore diameter (4V / A)
[0092] The microporous compound was further processed by (1) temperature and humidity conditioning and (2) steam impregnation. For temperature and humidity conditioning tests, the microporous compounds were placed in a conditioning chamber for 24 to 72 hours, where the temperature was controlled between 20°C and 30°C and the relative humidity was maintained between 50 and 98%. The PS / PAC25 compound particles ...
Embodiment 2
[0102] In the following samples and comparative samples, rigid polystyrene foam boards were produced by a twin-screw LMP extruder. Table 4 shows the processing operating conditions for the samples in the twin-screw extruder used to make foam boards with a width of 16 inches and a thickness of one inch.
[0103] Table 4
[0104] The processing conditions of the samples
[0105] Wt% of HFC-134a
4
CO 2 wt%
2
Injection pressure, Kpa(psi)
13000-17000(1950-2400)
Mold melting temperature (°C)
110-130
Die pressure, Kpa(psi)
6900-8280(1000-1200)
Linear speed, m / min (feet / min)
5-10(16-35)
Output, kg / h
150-200
Die gap, mm
0.8-1.5
Vacuum KPa(inch Hg)
0-3.4(0-16)
[0106] The results of Example 2 are summarized in Tables 5 and 6. Pore size was determined by Nikon Optiphot-2 light microscope and Clemex Vision image analysis software. Foam density was measured according to ASTM ...
Embodiment 3
[0114] The polystyrene resin used in this example was polystyrene (NOVA 1600 from NOVA Chemical Company, PA) with a melt index of about 5.2 and a molecular weight of 250,000. The microporous compound PS / PAC25 with the polystyrene.
[0115] Blowing agent carbon dioxide (from Praxair) was injected into the extruder at position L / D16 (melting and mixing zone) via a model ISCO1000D syringe pump. During the entire extrusion process, the temperature and pressure are maintained above the supercritical point, that is, the carbon dioxide remains in the supercritical stage before foaming at the end of the die.
[0116] Water is injected through a separate ISCO 1000D syringe pump at position L / D26 (transfer area) close to the die. During the extrusion process prior to foaming, water remains in liquid phase according to the water P-T phase diagram.
[0117] The recipes and corresponding pore sizes are listed in Table 7. In order to compare the effect of powdered activated carbon and ...
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