• 专利标题:   High-strength high temperature resistant MDI-based slow resilience polyurethane sponge comprises low-resilience polyether polyol, base polyether polyol, polymer polyor, high temperature reinforcing agent, amine catalyst, and tin catalyst.
  • 专利号:   CN113637319-A, CN113637319-B
  • 发明人:   WANG L, ZHENG Y
  • 专利权人:   UNIV FUZHOU
  • 国际专利分类:   C08G018/63, C08G018/48, C08J009/00, C08J009/08, C08K003/36, C08K003/04, C08K009/06, C08K009/02, C08L099/00, C08L003/06, C08L075/08
  • 专利详细信息:   CN113637319-A 12 Nov 2021 C08L-075/08 202205 Chinese
  • 申请详细信息:   CN113637319-A CN11040900 07 Sep 2021
  • 优先权号:   CN11040900

▎ 摘  要

NOVELTY - High-strength high temperature resistant MDI-based slow resilience polyurethane sponge comprises 40-60 pts. wt. low-resilience polyether polyol, 40-60 pts. wt. base polyether polyol, 0-20 pts. wt. polymer polyor, 1-5 pts. wt. high temperature reinforcing agent, 1.2-2.4 pts. wt. amine catalyst, 0.4-1.2 pts. wt. tin catalyst, 0.8-1.2 pts. wt. surface active agent, 1-2 pts.wt. foaming agent, 1-5 pts. wt. flame retardant and 30-65 pts. wt. methylene diphenyl diisocyanate. USE - High-strength high temperature resistant MDI-based slow resilience polyurethane sponge. ADVANTAGE - The high-strength high temperature resistant MDI-based slow resilience polyurethane sponge , greatly enhances the physical performance stability under high temperature, the flame retardance can reach the self-extinguishing of fire. DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing high-strength high temperature resistant MDI-based slow resilience polyurethane sponge, which involves mixing slow-resilience polyether polyol, base polyether polyol, polymer polyol, adding high temperature enhancer according to the formulation, amine catalyst, tin catalyst, surfactant; foaming agent, stirring for 30-60 seconds under the stirrer with the rotating speed of 1000-1500 r/min, marked as A component, adding the flame retardant filler, diphenyl methane diisocyanate into another container according to the proportion, stirring for 10-30 seconds under the stirrer with the rotating speed of 500-1000r/min, pouring the component B into a container filled with component A, stirring for 6-8 seconds under the stirrer with the rotating speed of 2500-3000 r/min; the system is white; pouring the system into the mould; controlling the temperature of the mould at 25 plus minus 0.5degrees Celsius; after 24-72 hours, cutting to obtain the product.