CN115703289A - Polyurethane foam product and preparation method of polyurethane foam - Google Patents
Polyurethane foam product and preparation method of polyurethane foam Download PDFInfo
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Abstract
Description
技术领域technical field
本发明涉及医疗器械及新材料制备领域,尤其涉及一种聚氨酯泡沫制品及聚氨酯泡沫的制备方法。The invention relates to the field of medical equipment and new material preparation, in particular to a polyurethane foam product and a preparation method of the polyurethane foam.
背景技术Background technique
聚氨酯泡沫是一种具有保温与防水功能的新型合成材料,具有较低的导热系数,硬质聚氨酯泡沫塑料主要应用在建筑物外墙保温,屋面防水保温一体化、冷库保温隔热、管道保温材料、建筑板材、冷藏车及冷库隔热材等。近年来,聚氨酯泡沫也越来越广泛的应用在医疗器械领域。一方面,现有技术中的聚氨酯泡沫,空隙直径较大,通常为100微米至350微米之间;另一方面,现有技术中聚氨酯泡沫的加工工艺较为复杂,生产成本较高。Polyurethane foam is a new type of synthetic material with thermal insulation and waterproof functions. It has a low thermal conductivity. Rigid polyurethane foam is mainly used in building exterior wall insulation, roof waterproof and thermal insulation integration, cold storage thermal insulation, and pipeline thermal insulation materials. , building panels, refrigerated trucks and cold storage insulation materials, etc. In recent years, polyurethane foam has become more and more widely used in the field of medical devices. On the one hand, the polyurethane foam in the prior art has a large void diameter, usually between 100 microns and 350 microns; on the other hand, the processing technology of the polyurethane foam in the prior art is relatively complicated, and the production cost is relatively high.
发明内容Contents of the invention
本发明的目的是提供一种聚氨酯泡沫制品及聚氨酯泡沫的制备方法。The object of the present invention is to provide a kind of polyurethane foam product and the preparation method of polyurethane foam.
本发明所提供的聚氨酯泡沫制品,所述聚氨酯泡沫制品内含有均匀分布的空隙,所述空隙的直径为5微米至30微米之间。In the polyurethane foam product provided by the present invention, the polyurethane foam product contains uniformly distributed voids, and the diameter of the voids is between 5 microns and 30 microns.
所述聚氨酯泡沫制品为厚度为3厘米矩形板状结构。所述聚氨酯泡沫制品包括聚氨酯泡沫制成的管状结构(1)。本发明所提供的聚氨酯泡沫制品,还设有一硬质内壁管(2)和一硬质外壁管(3);所述硬质内壁管(2)和所述硬质外壁管(3)同轴设置且二者之间具有环形空隙,所述聚氨酯泡沫制成的管状结构(1)夹设在所述硬质内壁管(2)和所述硬质外壁管(3)之间的环形空隙中。所述硬质内壁管(2)的轴长大于所述硬质外壁管(3)的轴长;所述硬质内壁管(2)的厚度为2毫米至3毫米之间;所述硬质外壁管(3)的厚度为0.8毫米至1毫米之间。The polyurethane foam product is a rectangular plate structure with a thickness of 3 cm. The polyurethane foam article comprises a tubular structure (1) made of polyurethane foam. The polyurethane foam product provided by the present invention is also provided with a hard inner wall pipe (2) and a hard outer wall pipe (3); the hard inner wall pipe (2) and the hard outer wall pipe (3) are coaxial There is an annular gap between the two, and the tubular structure (1) made of polyurethane foam is sandwiched in the annular gap between the hard inner wall tube (2) and the hard outer wall tube (3) . The axial length of the hard inner wall tube (2) is longer than the axial length of the hard outer wall tube (3); the thickness of the hard inner wall tube (2) is between 2 mm and 3 mm; the hard The thickness of the outer wall pipe (3) is between 0.8 mm and 1 mm.
本发明所提供的聚氨酯泡沫的制备方法,包括如下步骤:S1用于将聚氨酯预聚体和水相材料相混合,形成预制混合液的步骤;S2用于对预制混合液进行发泡处理使其发生发泡反应,从而生成发泡绵的步骤;S3用于对发泡绵进行烘干处理,从而得到聚氨酯泡沫的步骤。The preparation method of the polyurethane foam provided by the present invention comprises the following steps: S1 is used for mixing the polyurethane prepolymer and the water phase material to form a prefabricated mixed solution; S2 is used for foaming the prefabricated mixed solution to make it A foaming reaction occurs to generate a foam foam; S3 is used to dry the foam foam to obtain a polyurethane foam step.
所述S1用于将聚氨酯预聚体和水相材料相混合,形成预制混合液的步骤中,所述聚氨酯预聚体和水相材料的混合质量比例为1:1至1比0.4之间。所述S1用于将聚氨酯预聚体和水相材料相混合,形成预制混合液的步骤中,还包括用于使用高速搅拌仪器对预制混合液进行高速搅拌的步骤;所述用于使用高速搅拌仪器对预制混合液进行高速搅拌的步骤,在密闭隔绝空气的条件下进行;所述用于使用高速搅拌仪器对预制混合液进行高速搅拌的步骤,搅拌速度为3000转/分钟至5000转/分钟之间。所述S1用于将聚氨酯预聚体和水相材料相混合,形成预制混合液的步骤中,所述聚氨酯预聚体的温度为25摄氏度至35摄氏度之间,所述水相材料的温度为0摄氏度至10摄氏度之间;所述S2用于对预制混合液进行发泡处理使其发生发泡反应,从而生成发泡绵的步骤,其发泡处理的温度为25摄氏度至60摄氏度之间;所述S3用于对发泡绵进行烘干处理,从而得到聚氨酯泡沫的步骤中,烘干温度为100摄氏度至150摄氏度之间。所述聚氨酯预聚体采用甲苯二异氰酸酯和聚醚多元醇反应制得;所述水相材料由水、表面活性剂、匀泡剂和开孔剂混合组成;所述表面活性剂采用有机硅表面活性剂;所述匀泡剂采用环氧乙烷聚合物;所述开孔剂采用有机硅聚合物、微粉硅胶或氧化丙烯氧化乙烯丙二醇醚中的一种、两种或三种的组合。The S1 is used in the step of mixing the polyurethane prepolymer and the water phase material to form a prefabricated mixed liquid, and the mixing mass ratio of the polyurethane prepolymer and the water phase material is between 1:1 and 1:0.4. The S1 is used for mixing the polyurethane prepolymer and the water phase material to form a prefabricated mixed solution, and also includes a step for using a high-speed stirring instrument to perform high-speed agitation on the prefabricated mixed solution; The step of high-speed stirring of the prefabricated mixed solution by the instrument is carried out under the condition of airtight isolation; the step of using a high-speed stirring instrument to perform high-speed stirring of the prefabricated mixed solution, the stirring speed is 3000 rpm to 5000 rpm between. The S1 is used for mixing the polyurethane prepolymer and the water phase material to form a prefabricated mixed solution, the temperature of the polyurethane prepolymer is between 25 degrees Celsius and 35 degrees Celsius, and the temperature of the water phase material is Between 0 degrees Celsius and 10 degrees Celsius; the S2 is used to foam the prefabricated mixed solution to cause a foaming reaction to generate a foaming sponge, and the temperature of the foaming treatment is between 25 degrees Celsius and 60 degrees Celsius ; The S3 is used for drying the foamed cotton to obtain polyurethane foam, and the drying temperature is between 100 degrees Celsius and 150 degrees Celsius. The polyurethane prepolymer is prepared by reacting toluene diisocyanate and polyether polyol; the water phase material is composed of water, surfactant, foam stabilizer and cell opener; the surfactant is made of silicone surface Active agent; the foam stabilizer adopts ethylene oxide polymer; the cell opening agent adopts one, two or three combinations of organosilicon polymer, micropowder silica gel or oxypropylene oxide ethylene propylene glycol ether.
本发明所提供的聚氨酯泡沫制品,空隙的直径为5微米至30微米之间,具有更低的导入系数,保温保冷性能更佳。本发明所提供的聚氨酯泡沫的制备方法,可将生成的聚氨酯泡沫的孔径控制在5微米至30微米之间,均匀度佳,开孔性能优异,可获得具有较佳乳胶感和舒适感的聚氨酯泡沫,在保证生产效率的同时,可有效降低生产成本。In the polyurethane foam product provided by the invention, the diameter of the voids is between 5 microns and 30 microns, has a lower introduction coefficient, and has better heat preservation and cold preservation performance. The preparation method of polyurethane foam provided by the present invention can control the pore diameter of the generated polyurethane foam between 5 microns and 30 microns, has good uniformity, excellent cell opening performance, and can obtain polyurethane with better latex feeling and comfortable feeling. Foam, while ensuring production efficiency, can effectively reduce production costs.
附图说明Description of drawings
图1为本发明实施例一所述的聚氨酯泡沫制品的结构示意图;Fig. 1 is the structural representation of the polyurethane foam product described in the first embodiment of the present invention;
图2为本发明实施例二所述的聚氨酯泡沫的制备方法的步骤示意图。Fig. 2 is a schematic diagram of the steps of the method for preparing polyurethane foam described in Example 2 of the present invention.
具体实施方式Detailed ways
为使本发明实施例的目的、技术方案和优点更加清楚,下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments It is a part of embodiments of the present invention, but not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
实施例一Embodiment one
本实施例提供一种聚氨酯泡沫制品,所述聚氨酯泡沫制品内含有均匀分布的空隙,所述空隙的直径为5微米至30微米之间。本领域技术人员可以理解,所述聚氨酯泡沫制品的孔径设置为5微米至30微米之间,可使得该聚氨酯泡沫制品具有较佳的绝热性能,可使用在具有较高保温或保冷要求的医疗器械中。This embodiment provides a polyurethane foam product, the polyurethane foam product contains uniformly distributed voids, and the diameter of the voids is between 5 microns and 30 microns. Those skilled in the art can understand that the pore size of the polyurethane foam product is set between 5 microns and 30 microns, which can make the polyurethane foam product have better heat insulation performance, and can be used in medical devices with higher heat preservation or cold preservation requirements middle.
进一步,本实施例所提供的聚氨酯泡沫制品为厚度为3厘米矩形板状结构。本领域技术人员可以理解,将本实施例所提供的聚氨酯泡沫切割为3厘米矩形板状,便于运输、堆叠和存储,便于后续加工使用。Furthermore, the polyurethane foam product provided in this embodiment is a rectangular plate structure with a thickness of 3 cm. Those skilled in the art can understand that cutting the polyurethane foam provided in this embodiment into a 3 cm rectangular plate is convenient for transportation, stacking and storage, and for subsequent processing and use.
进一步,本实施例所提供的聚氨酯泡沫制品包括聚氨酯泡沫制成的管状结构1。本领域技术人员可以理解,所述聚氨酯泡沫制成的管状结构1可以用于医疗器械或医疗设备中的保温管材使用。Further, the polyurethane foam product provided in this embodiment includes a tubular structure 1 made of polyurethane foam. Those skilled in the art can understand that the tubular structure 1 made of polyurethane foam can be used as a heat-insulating pipe in medical equipment or medical equipment.
进一步,本实施例所提供的聚氨酯泡沫制品还设有一硬质内壁管2和一硬质外壁管3;所述硬质内壁管2和所述硬质外壁管3同轴设置且二者之间具有环形空隙,所述聚氨酯泡沫制成的管状结构1夹设在所述硬质内壁管2和所述硬质外壁管3之间的环形空隙中。本领域技术人员可以理解,在聚氨酯泡沫制成的管状结构1的内壁侧和外壁侧设置硬质管,可将需保温处理的介质如液体,直接放置在内壁管内;所述硬质外壁管3可对聚氨酯泡沫制成的管状结构1起到保护作用,防止其变形和收到外界环境碰、撞、刮、切等损害。Further, the polyurethane foam product provided in this embodiment is also provided with a hard
进一步,所述硬质内壁管2的轴长大于所述硬质外壁管3的轴长。本领域技术人员可以理解,这样所述硬质内壁管2凸出于所述硬质外壁管3和硬质外壁管3,便于进行装配。Further, the axial length of the rigid
进一步,所述硬质内壁管2的厚度为2毫米至3毫米之间。本领域技术人员可以理解,将硬质内壁管2的厚度设置为2毫米至3毫米之间,既可保证所述硬质内壁管2达到使用需求也同时保证其具有较轻的重量和较低的制造成本。Further, the thickness of the hard
进一步,所述硬质外壁管3的厚度为0.8毫米至1毫米之间。本领域技术人员可以理解,将硬质外壁管3的厚度设置为0.8毫米至1毫米之间,既可保证所述硬质外壁管3达到使用需求也同时保证其具有较轻的重量和较低的制造成本。Further, the thickness of the hard
实施例二Embodiment two
本实施例提供一种聚氨酯泡沫的制备方法,包括如下步骤:The present embodiment provides a kind of preparation method of polyurethane foam, comprises the steps:
S1用于将聚氨酯预聚体和水相材料相混合,形成预制混合液的步骤;S1 is a step for mixing the polyurethane prepolymer and the water phase material to form a prefabricated mixed solution;
S2用于对预制混合液进行发泡处理使其发生发泡反应,从而生成发泡绵的步骤;S2 is a step for foaming the prefabricated mixed solution to cause a foaming reaction to generate foam;
S3用于对发泡绵进行烘干处理,从而得到聚氨酯泡沫的步骤。S3 is a step for drying the foamed cotton to obtain polyurethane foam.
进一步,所述S1用于将聚氨酯预聚体和水相材料相混合,形成预制混合液的步骤中,所述聚氨酯预聚体和水相材料的混合质量比例为1:1至1比0.4之间。本领域技术人员可以理解,将聚氨酯预聚体和水相材料的混合质量比例为1:1至1比0.4之间,可将生成的聚氨酯泡沫内的空隙的孔径控制在5微米至30微米之间。Further, the S1 is used for mixing the polyurethane prepolymer and the water phase material to form a prefabricated mixed solution, the mixing mass ratio of the polyurethane prepolymer and the water phase material is between 1:1 and 1:0.4 between. Those skilled in the art can understand that if the mixing mass ratio of the polyurethane prepolymer and the water phase material is between 1:1 and 1:0.4, the pore size of the pores in the generated polyurethane foam can be controlled between 5 microns and 30 microns between.
进一步,所述S1用于将聚氨酯预聚体和水相材料相混合,形成预制混合液的步骤中,还包括用于使用高速搅拌仪器对预制混合液进行高速搅拌的步骤。本领域技术人员可以理解,这样可增加预制混合液的均匀度,使得生成的发泡绵质量更加均匀稳定。Further, the step of S1 for mixing the polyurethane prepolymer and the water phase material to form a prefabricated mixed solution also includes a step of using a high-speed stirring device to perform high-speed stirring on the prefabricated mixed solution. Those skilled in the art can understand that this can increase the uniformity of the prefabricated mixture, making the quality of the resulting foam more uniform and stable.
进一步,所述用于使用高速搅拌仪器对预制混合液进行高速搅拌的步骤,在密闭隔绝空气的条件下进行。本领域技术人员可以理解,在密闭隔绝空气的条件下进行高速搅拌,可防止在搅拌过程中混入空气形成气泡,从而造成生成发泡不均,导致生成的聚氨酯泡沫内部结构均匀度差,隔热性能差。Further, the step of using a high-speed stirring device to high-speed stir the prefabricated mixed solution is carried out under the condition of airtight isolation. Those skilled in the art can understand that high-speed stirring under airtight and air-isolated conditions can prevent air from being mixed in the stirring process to form air bubbles, resulting in uneven foaming, resulting in poor uniformity of the internal structure of the polyurethane foam generated, and heat insulation. Poor performance.
进一步,所述用于使用高速搅拌仪器对预制混合液进行高速搅拌的步骤,搅拌速度为3000转/分钟至5000转/分钟之间。Further, in the step of using a high-speed stirring device to stir the prefabricated mixed solution at a high speed, the stirring speed is between 3000 rpm and 5000 rpm.
进一步,所述S1用于将聚氨酯预聚体和水相材料相混合,形成预制混合液的步骤中,所述聚氨酯预聚体的温度为25摄氏度至35摄氏度之间,所述水相材料的温度为0摄氏度至10摄氏度之间。Further, the S1 is used for mixing the polyurethane prepolymer and the water phase material to form a prefabricated mixed solution, the temperature of the polyurethane prepolymer is between 25 degrees Celsius and 35 degrees Celsius, and the water phase material The temperature is between 0°C and 10°C.
进一步,所述S2用于对预制混合液进行发泡处理使其发生发泡反应,从而生成发泡绵的步骤,其发泡处理的温度为25摄氏度至60摄氏度之间。本领域技术人员可以理解,将发泡处理的温度设置为25摄氏度至60摄氏度之间,既可保证发泡效果,将孔径控制在5微米至30微米之间,有可保证发泡处理具有较短的时间,确保具有较高的生产效率。Further, the step of S2 is used for foaming the prefabricated mixed solution to cause a foaming reaction to generate a foam, and the temperature of the foaming treatment is between 25 degrees Celsius and 60 degrees Celsius. Those skilled in the art can understand that setting the temperature of the foaming treatment between 25 degrees Celsius and 60 degrees Celsius can ensure the foaming effect, and controlling the pore size between 5 microns and 30 microns can ensure that the foaming process has a better effect. Short time ensures high production efficiency.
进一步,所述S3用于对发泡绵进行烘干处理,从而得到聚氨酯泡沫的步骤中,烘干温度为100摄氏度至150摄氏度之间。本领域技术人员可以理解,将烘干温度设置在100摄氏度至150摄氏度之间,可保证烘干效果的前提下,烘干时间较短,具有较佳的生产效率。Further, the S3 is used for drying the foamed cotton to obtain the polyurethane foam, and the drying temperature is between 100°C and 150°C. Those skilled in the art can understand that setting the drying temperature between 100°C and 150°C can guarantee the drying effect, shorten the drying time, and have better production efficiency.
进一步,所述S1用于将聚氨酯预聚体和水相材料相混合,形成预制混合液的步骤中,所述聚氨酯预聚体可采用甲苯二异氰酸酯(TDI,Toluene diisocyanate)和聚醚多元醇反应制得。Further, the S1 is used to mix the polyurethane prepolymer and the water phase material to form a prefabricated mixed solution. The polyurethane prepolymer can be reacted with toluene diisocyanate (TDI, Toluene diisocyanate) and polyether polyol be made of.
进一步,所述水相材料由水、表面活性剂、匀泡剂和开孔剂混合组成。Further, the water phase material is composed of water, surfactant, foam stabilizer and cell opener.
进一步,所述表面活性剂可采用有机硅表面活性剂。Further, the surfactant can be an organosilicon surfactant.
进一步,所述匀泡剂可采用环氧乙烷聚合物。Further, the foam stabilizer can use ethylene oxide polymer.
进一步,所述开孔剂可以采用有机硅聚合物、微粉硅胶或氧化丙烯氧化乙烯丙二醇醚(KF-28)中的一种、两种或三种的组合。本领域技术人员可以理解,所述有机硅聚合物又称聚硅氧烷,聚硅醚。有机硅聚合物在Si原子上接有碳侧链的聚合物。有机硅聚合物根据其分子量的高低而呈液态、半固态或固态。有机硅聚合物按其形态和用途,可分为硅油、硅树脂和硅橡胶三大类。硅油是由单官能团和双官能团的甲基、乙基或苯基氯硅烷等经水解缩聚而制成的线型结构的油状液体。硅树脂由双官能和三官能团单体按一定配比进行水解的预聚体生成的线型聚合物,可进行交联固化反应,成为热固性网状立体结构的硅树脂。硅橡胶是由极纯的双官能团单体经水解缩聚而成,平均分子量在为线型结构。无论是液体、固体或弹性体的聚硅氧烷均有很高的电绝缘性、憎水性、耐热性、耐寒性。本领域技术人员可以理解,微粉硅胶是白色粉末状的无机化工产品。微粉硅胶无毒、无味、不燃、不爆、不挥发、无腐蚀、孔容大、表面活性强。微粉硅胶化学性质稳定,不溶于水。本领域技术人员可以理解,采用上述开孔剂,可使得本实施来所生成的聚氨酯泡沫具有较高的回弹性能,可有效增加发泡工艺的宽容度,具有优异的开孔性,防止闭孔,可有效改善聚氨酯泡沫结构,有效提高聚氨酯泡沫材料的乳胶感和舒适感。Further, the pore opener can be one, two or three combinations of organosilicon polymer, micropowder silica gel or propylene oxide propylene glycol ether (KF-28). Those skilled in the art can understand that the organosilicon polymer is also called polysiloxane or polysiloxane. Silicone polymers are polymers with carbon side chains attached to Si atoms. Silicone polymers are liquid, semi-solid or solid depending on their molecular weight. Silicone polymers can be divided into three categories according to their form and use: silicone oil, silicone resin and silicone rubber. Silicone oil is an oily liquid with a linear structure produced by hydrolysis and polycondensation of monofunctional and difunctional methyl, ethyl or phenyl chlorosilanes. Silicone resin is a linear polymer produced by hydrolyzing prepolymers of bifunctional and trifunctional monomers in a certain proportion, which can undergo crosslinking and curing reactions to become a silicone resin with a thermosetting network three-dimensional structure. Silicone rubber is formed by hydrolysis and polycondensation of extremely pure bifunctional monomers, with an average molecular weight of is a linear structure. Polysiloxane, whether it is liquid, solid or elastomer, has high electrical insulation, water repellency, heat resistance, and cold resistance. Those skilled in the art can understand that micronized silica gel is a white powdery inorganic chemical product. Micro-powder silica gel is non-toxic, tasteless, non-flammable, non-explosive, non-volatile, non-corrosive, large pore volume, and strong surface activity. Micropowder silica gel is chemically stable and insoluble in water. Those skilled in the art can understand that the use of the above-mentioned cell-opening agent can make the polyurethane foam generated in this practice have higher resilience performance, effectively increase the tolerance of the foaming process, have excellent cell-opening properties, and prevent closed cells. Holes can effectively improve the polyurethane foam structure, effectively improve the latex feel and comfort of polyurethane foam materials.
最后应说明的是:以上实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的精神和范围。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: it can still be Modifications are made to the technical solutions described in the foregoing embodiments, or equivalent replacements are made to some of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the spirit and scope of the technical solutions of the various embodiments of the present invention.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006001013A (en) * | 2004-06-15 | 2006-01-05 | Inoac Corp | Foamed polyurethane sheet with support and its manufacturing method |
JP2006124579A (en) * | 2004-10-29 | 2006-05-18 | Inoac Corp | Polyurethane foam and method for producing the same |
CN105542116A (en) * | 2014-10-31 | 2016-05-04 | 郁丁丁 | Novel carbon fiber-reinforced polyurethane hard foam plastic preparation method |
CN207094072U (en) * | 2017-08-08 | 2018-03-13 | 厦门同力节能科技有限公司 | A kind of insulating tube |
-
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006001013A (en) * | 2004-06-15 | 2006-01-05 | Inoac Corp | Foamed polyurethane sheet with support and its manufacturing method |
JP2006124579A (en) * | 2004-10-29 | 2006-05-18 | Inoac Corp | Polyurethane foam and method for producing the same |
CN105542116A (en) * | 2014-10-31 | 2016-05-04 | 郁丁丁 | Novel carbon fiber-reinforced polyurethane hard foam plastic preparation method |
CN207094072U (en) * | 2017-08-08 | 2018-03-13 | 厦门同力节能科技有限公司 | A kind of insulating tube |
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