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Improvements in or relating to a method of carrying out reactions for the conversion of liquid materials into solid or semi-solid products

机译:对进行反应的方法的改进,该方法用于将液态物质转化为固体或半固体产物

摘要

PICT:0445478/IV/1 Methacrylic acid esters or mixtures thereof are polymerized to produce formed articles such as plates, bars or strips, by carrying out the polymerization in relatively narrow chambers which are subjected over most of their surface to the action of a temperature regulating medium, which may be gaseous or, preferably, liquid, and controlling the temperature of said medium. The temperature of the medium may be first adjusted so as to bring the contents of the chambers to the required temperature for carrying out the polymerization, e.g. 70 DEG C., after which, if the reaction is exothermic, the heat of reaction may be conducted away by suitably controlling the temperature of the regulating medium. Before introduction into the chambers the starting materials may be freed from bubbles, e.g. by evacuation, heating or boiling. The reaction may be carried out in flat chambers, e.g. of metal, of say 2--3 mm. or up to 10 mm. or in some cases even greater thickness, which are subjected to the action of the temperature regulating medium on all faces or on their two flat sides. A plurality of such chambers may be combined into a system of chambers separated by interspaces through which the temperature regulating medium circulates, or such a system may be built up from a plurality of frames. After completion of the reaction, the product is removed from the chambers, e.g. by removing one side or one edge and allowing the plate to fall out. Removal of the products may be facilitated by providing between the reaction product and the walls a separating layer, e.g. of viscose, gelatine or glue or of paper or woven material preferably impregnated with glue or gelatine, which separating layers may be in the form of bags or envelopes which, after being filled with the material to be polymerized, may be closed by folding over the upper part, and in which the polymer may be subsequently stored or transported. Instead of being flat, the chambers may be in the form of tubes of cylindrical, oval or square cross - section, which can be subjected over the whole or almost the whole of their surface to the action of a heating medium. In the apparatus shown, the polymerization chambers are formed of frames b between heat regulating chambers a to which the regulating medium is supplied by pipes c and from which it is withdrawn by pipes d. The system is supported by rollers k on a frame or on rails f, and is pressed together between heads h, h1 and the spindle g, whilst each pair of chambers may be connected by quick acting connections, e.g. hooks or chains. The frames may be rectangular, oval, square or circular, and the side faces of the regulating chambers may be flat or may have raised or depressed portions to produce suitable shapes in the polymer, e.g. they may be grooved or fluted so as to enclose a tubular space. The reaction chambers are filled through pipes e by suction or by application of pressure, and in the latter case the pressure may be maintained during polymerization. The products may be employed in the form in which they are produced, e.g. as glass substitutes, or may be shaped into other forms, e.g. plates may be placed between metal plates of larger dimensions and subjected to heat and pressure to produce thinner plates of larger area. The products may also be employed for the manufacture of safety glass. Products in the form of rods may be cut into small plates of suitable thickness, e.g. 0,5 mm. to 1 cm., which may be placed between metal or glass plates and heated and pressed into thinner layers, e.g. of 0,05 to 0,2 mm. thickness, producing round or oval artificial glass discs or discs of splinterless glass for optical purposes, e.g. for protective spectacles or goggles. In examples: (1) methacrylic acid ethyl ester, mixed with a softening-agent, e.g. isobutyl phthalate, and an accelerator, e.g. benzoyl peroxide, is heated in flat chambers 5 mm. thick at 70 DEG C.; (2) a mixture of methacrylic acid ethyl and methyl esters with the addition of isobutyl phthalate is similarly polymerized in layers 10 mm. thick; (3) methacrylic acid ethyl ester alone is polymerized as in (1). The Specification as open to inspection under Sect. 91 comprises the application of the process and apparatus to any reaction for the conversion of liquid materials into solid or semisolid products, e.g. the polymerization of unsaturated organic compounds such as esters of acrylic acid, vinyl acetate or styrene, or condensation reactions such as the manufacture of phenol-aldehyde condensation products. In an additional example, vinyl acetate is polymerized as in (1) above. An application of the process to the production of safety glass is described in which a monomeric or partially polymerized product is polymerized between two glass plates secured together by a strip of elastic yielding material (e.g. a rubber-like polymerization product, a polymerization product of methyl acrylate, paper or rubber) interrupted so as to provide an opening for the introduction of the liquid to be polymerized. Alternatively, a number of small elastic discs are placed at intervals round the edges of the space between the plates, and three of the edges are closed in a liquid tight manner, e.g. by means of paper. Safety glass may also be produced by placing a comparatively thick sheet of polymerization product symmetrically between two sheets of glass of greater area and applying pressure until the polymerization product is compressed to a thinner sheet of area sufficient to fill the space between the plates. This subject-matter does not appear in the Specification as accepted.ALSO:PICT:0445478/III/1 The polymerization of methacrylic acid esters is carried out in relatively narrow chambers which are subjected over most of their surface to the action of a temperature regulating medium, which may be gaseous or, preferably, liquid. The reaction chambers may be flat chambers, e.g. of metal, of say 2--3 mm. or up to 10 mm. or in some cases even greater thickness, and may be subjected to the action of the temperature regulating medium on all faces or on their flat sides. A plurality of such chambers may be combined into a system of chambers separated by interspaces through which the temperature regulating medium circulates, or such a system may be built up from a plurality of frames. In order to facilitate the removal of the product after the reaction, there may be provided between the reaction product and the walls a separating layer, e.g. of viscose, gelatine or glue or of paper or woven material preferably impregnated with glue or gelatine, which separating layers may be in the form of bags or envelopes which, after being filled with the material to be polymerized, may be closed by folding over the upper part. Instead of being flat, the chambers may be in the form of tubes of cylindrical, oval or square cross-section, which can be subjected over the whole or almost the whole of their surface to the action of a heating medium. In the apparatus shown in the drawings, the polymerization chambers are formed of frames b between heat regulating chambers a to which the regulating medium is supplied by pipes c and from which it is withdrawn by pipes d. The system is supported by rollers k on a frame or on rails f, and is pressed together between heads h, h1 and the spindle g, whilst each pair of chambers may be connected by quick acting connections, e.g. hooks or chains. The frames may be rectangular, oval, square or circular, and the side faces of the regulating chambers may be flat or may have raised or depressed portions to produce suitable shapes in the polymer, e.g. they may be grooved or fluted so as to enclose a tubular space. The reaction chambers are filled through pipes e by suction or by application of pressure. The Specification as open to inspection under Sect. 91 comprises the application of the process and apparatus to polymerization reactions in general. This subject-matter does not appear in the Specification as accepted.
机译:通过在相对狭窄的小室中进行聚合反应,使甲基丙烯酸酯或其混合物聚合,以形成成形品,例如板,条或条,该小室在其大部分表面上经受着丙烯腈的作用。温度调节介质,其可以是气态或优选为液体,并控制所述介质的温度。可以首先调节介质的温度,以使腔室中的内容物达到进行聚合所需的温度,例如3℃。 70℃后,如果反应放热,则可通过适当控制调节介质的温度将反应热带走。在引入腔室之前,可以使起始材料不含气泡,例如气泡。通过疏散,加热或煮沸。该反应可以在平坦的室中进行,例如金属,例如2--3毫米。或最大10毫米。或者在某些情况下甚至更大的厚度,这些温度在所有面或在其两个平坦侧面上都受到温度调节介质的作用。多个这样的腔室可以组合成由间隔空间分隔的腔室系统,温度调节介质循环通过该间隔空间,或者可以由多个框架来构建这样的系统。反应完成后,将产物从室中移出,例如从反应器中取出。移开一侧或一条边缘,让板掉出。通过在反应产物和壁之间提供分离层,例如有机层,可以促进产物的去除。粘胶,明胶或胶水或纸或机织材料的材料,最好用胶水或明胶浸渍,其分离层可以是袋或信封的形式,在装满要聚合的材料后,可通过折叠将其封闭上部,随后可以在其中存储或运输聚合物。这些腔室可以不是圆柱形的而是圆柱形,椭圆形或正方形横截面的管的形式,其可以在其整个表面或几乎整个表面上经受加热介质的作用。在所示的设备中,聚合室由框架b构成,框架b位于热调节室a之间,通过管道c将调节介质供应至该调节介质,并通过管道d将其从中抽出。该系统由框架或轨道f上的滚子k支撑,并且在头h,h 1和主轴g之间被压在一起,而每对腔室可以通过快速作用的连接来连接。钩子或链子。框架可以是矩形,椭圆形,正方形或圆形,并且调节腔室的侧面可以是平坦的,或者可以具有凸起或凹陷的部分以在聚合物中产生合适的形状,例如形状。它们可以开槽或开槽以便封闭管状空间。反应室通过抽吸或施加压力通过管道e填充,并且在后一种情况下,可以在聚合过程中保持压力。产品可以以其生产的形式使用,例如。作为玻璃替代品,或者可以成型为其他形式,例如可将板放置在较大尺寸的金属板之间,并经受热和压力以产生较大面积的较薄板。该产品还可用于生产安全玻璃。棒状产品可以切成合适厚度的小板,例如0.5毫米至1厘米,可放置在金属或玻璃板之间,加热并压成较薄的层,例如0.05至0.2毫米厚度,生产用于光学目的的圆形或椭圆形人造玻璃圆盘或无碎片玻璃圆盘,例如用于防护眼镜或护目镜。在实施例中:(1)甲基丙烯酸乙酯,与一种软化剂混合,例如一种或多种。邻苯二甲酸异丁酯和促进剂,例如将过氧化苯甲酰在5 mm的平面室内加热。在70℃下厚; (2)将甲基丙烯酸乙酯和甲酯与邻苯二甲酸异丁酯加成的混合物类似地在10mm的层中聚合。厚; (3)单独地如(1)那样聚合甲基丙烯酸乙酯。该规范可供本节检查。图91的方法包括将该方法和设备应用于将液体材料转化成固体或半固体产物,例如固体产物的任何反应。不饱和有机化合物的聚合,例如丙烯酸,乙酸乙烯酯或苯乙烯的酯,或缩合反应,例如酚醛缩合产物的生产。在另一个实例中,乙酸乙烯酯如上述(1)中那样聚合。描述了该方法在生产安全玻璃中的应用,其中单体或部分聚合的产物在通过弹性屈服材料条固定在一起的两个玻璃板之间聚合(例如橡胶状聚合产物,甲基的聚合产物)。丙烯酸酯,纸或橡胶)打断,以便为引入要聚合的液体提供开口。可替代地,在板之间的空间的边缘周围以一定间隔布置多个小的弹性盘,并且以液体密封的方式(例如,以不透水的方式)封闭三个边缘。用纸的方式。也可以通过将相对较厚的聚合产物片对称地放置在两块较大面积的玻璃片之间并施加压力,直到聚合产物被压缩到足以填满板之间空间的较薄的面积片来生产安全玻璃。该主题未出现在所接受的规范中。ALSO:甲基丙烯酸酯的聚合是在相对狭窄的小室中进行的,该小室在其大部分表面上都受到酸的作用。温度调节介质,其可以是气体或优选为液体。反应室可以是平坦的室,例如。金属,例如2--3毫米。或最大10毫米。甚至在某些情况下甚至更大的厚度,并且可能在所有面上或在其平坦侧面上受到温度调节介质的作用。多个这样的腔室可以组合成由间隔空间分开的腔室系统,温度调节介质循环通过该间隔系统,或者这种系统可以由多个框架构成。为了促进反应后产物的去除,可以在反应产物和壁之间设置分离层,例如分离层。粘胶,明胶或胶水或纸或机织材料(最好浸渍有胶水或明胶)制成的隔离层,可以是袋或信封的形式,在装满要聚合的材料后,可以折叠在纸上以使其封闭上面的部分。这些腔室可以不是圆柱形的而是圆柱形,椭圆形或正方形的横截面,其可以在其整个表面或几乎整个表面上经受加热介质的作用。在附图所示的装置中,聚合室由在调温室a之间的框架b形成,通过管c向调节室a供应调节介质,并通过管d将调节介质从中抽出。该系统由框架或轨道f上的滚子k支撑,并且在头h,h 1和主轴g之间被压在一起,而每对腔室可以通过快速作用的连接来连接。钩子或链子。框架可以是矩形,椭圆形,正方形或圆形,并且调节腔室的侧面可以是平坦的,或者可以具有凸起或凹陷的部分以在聚合物中产生合适的形状,例如形状。它们可以开槽或开槽以便封闭管状空间。通过抽吸或施加压力通过管道e填充反应室。该规范可供本节检查。图91的流程图包括将该方法和设备通常应用于聚合反应。该主题未在接受的规范中出现。

著录项

  • 公开/公告号GB445478A

    专利类型

  • 公开/公告日1936-04-09

    原文格式PDF

  • 申请/专利权人 OTTO ROHM;

    申请/专利号GB19340028943

  • 发明设计人

    申请日1934-10-09

  • 分类号C08F20/12;

  • 国家 GB

  • 入库时间 2022-08-24 06:05:19

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