Process for the production of an elastomer-filler mixture optionally
containing extender oils
    1.
    发明授权
    Process for the production of an elastomer-filler mixture optionally containing extender oils 失效
    制备任选含有增量油的弹性体 - 填料混合物的方法

    公开(公告)号:US4366285A

    公开(公告)日:1982-12-28

    申请号:US282772

    申请日:1981-07-13

    摘要: A process for producing an elastomer-filler mixture optionally containing an extender oil, comprising the combined precipitation of a homogeneous mixture of a synthetic elastomer latex, produced by emulsion polymerization in an anionic emulsifier system, and an aqueous suspension of a silicic acid based filler, using an acid and, optionally, an electrolyte or other flocculant; separation of the precipitated mixture; and drying of the mixture; is improved in that the filler suspension contains 0.1-5% by weight, based on the amount of filler, of a copolymer of acrylamide and dimethylaminoethyl methacrylate.

    摘要翻译: 一种制备任选地含有增量油的弹性体 - 填料混合物的方法,包括通过在阴离子乳化剂体系中通过乳液聚合制备的合成弹性体胶乳的均匀混合物与硅酸基填料的水性悬浮液的组合沉淀, 使用酸和任选的电解质或其它絮凝剂; 分离沉淀的混合物; 并干燥混合物; 改进之处在于填料悬浮液含有0.1-5重量%,基于填料的量,丙烯酰胺和甲基丙烯酸二甲基氨基乙酯的共聚物。

    Hot-melt adhesive copolyamide having resistance to engine fuels
    3.
    发明授权
    Hot-melt adhesive copolyamide having resistance to engine fuels 失效
    具有耐发动机燃料的热熔性粘合剂共聚酰胺

    公开(公告)号:US4386197A

    公开(公告)日:1983-05-31

    申请号:US155670

    申请日:1980-06-02

    摘要: Hot-melt adhesives for articles which come into contact with organic fuels for internal engines comprising binary copolyamides having:A. 50-90 percent by weight of lactams or .omega.-aminocarboxylic acids having at least 10 methylene groups; andB. 50-10 percent by weight of equimolar quantities of aliphatic dicarboxylic acids and of aliphatic or cycloaliphatic diamines in which the total of the methyl, methylene and/or methylidyne groups present is at least 13.The extractable content in the copolyamide hot-melt adhesive is not more than 5 percent by weight as determined after 9 hours in boiling ethanol.

    摘要翻译: 与用于内部发动机的有机燃料接触的制品的热熔粘合剂包括二元共聚酰胺,其具有:A. 50-90重量%的具有至少10个亚甲基的内酰胺或ω-氨基羧酸; 和B.50-10重量%的等摩尔量的脂族二羧酸和脂族或脂环族二胺,其中存在的甲基,亚甲基和/或甲基炔基的总数为至少13.共聚酰胺热塑性树脂中的可萃取的含量, 熔融粘合剂在沸腾乙醇中9小时后测定不超过5重量%。

    Process for the recovery of pure methylal from methanol-methylal mixtures
    4.
    发明授权
    Process for the recovery of pure methylal from methanol-methylal mixtures 失效
    从甲醇 - 甲缩醛混合物中回收纯甲缩醛的方法

    公开(公告)号:US4385965A

    公开(公告)日:1983-05-31

    申请号:US342975

    申请日:1982-01-26

    CPC分类号: C07C41/58

    摘要: In a process for recovering pure methylal from methanol-methylal mixtures, which can optionally contain still further compounds, the separation conducted in a rectification device comprising two rectifying columns. In the first rectifying column, the mixture to be separated is rectified under a pressure lower than that in the second column, into a methylal-rich, methanol-poor distillate, and into a practically methylal-free, methanol-rich sump product. The methylal-rich distillate of the first rectification is then separated in a second rectifying column, operated under a higher pressure than the first rectification column, into a compound stream containing methanol and methylal, which is then recycled to the first rectifying column, and into pure methylal as the sump product. In a specific refinement, the first rectification is preferably operated under a pressure of 1-22 bar absolute and the second rectification preferably under a pressure of 9-30 bar absolute, with the second rectification being operated under a pressure which is at least 8 bar higher than that of the first rectification.

    摘要翻译: 在从可以任选地含有其它化合物的甲醇 - 甲缩醛混合物中回收纯甲缩醛的方法中,在包括两个精馏塔的精馏装置中进行分离。 在第一精馏塔中,将待分离的混合物在低于第二塔的压力下进行精馏,成为富含甲缩醛的不饱和甲醇的馏出物,并进入实际上无甲醛的富含甲醇的油槽产物。 然后将第一精馏的甲缩醛馏出物在比第一精馏塔高的压力下操作的第二精馏塔中分离成含有甲醇和甲缩醛的复合物流,然后将其再循环至第一精馏塔,并进入 纯甲缩醛作为贮槽产品。 在特定的改进中,第一精馏优选在1-22巴绝对压力下操作,优选在9-30巴绝对压力下进行第二次精馏,第二次精馏在至少8巴的压力下操作 高于首次整改。

    Process for uniformly blending additives into thermoplastic synthetic
resins
    5.
    发明授权
    Process for uniformly blending additives into thermoplastic synthetic resins 失效
    将添加剂均匀混合到热塑性合成树脂中的方法

    公开(公告)号:US4366270A

    公开(公告)日:1982-12-28

    申请号:US096428

    申请日:1979-11-21

    申请人: Jorn Ruter

    发明人: Jorn Ruter

    摘要: A method for the uniform blending of additives into thermoplastic synthetic resins. A solution or finely divided dispersion of the additive is produced in a polymerizable cyclic ester of the general formula: ##STR1## wherein R represents respectively hydrogen or an alkyl group of 1-18 carbon atoms,A represents a --O-- or --COO-- group,x and y represent integers from 1 to 15, andz represents 0 or 1.This solution or dispersion, optionally after polymerization of the cyclic ester, is admixed to the thermoplastic synthetic resin at the end of its manufacturing process or in a subsequent processing stage.

    摘要翻译: 将添加剂均匀混合到热塑性合成树脂中的方法。 在具有下列通式的可聚合环状酯中产生添加剂的溶液或细分散体:其中R表示氢或1-18个碳原子的烷基,A表示-O-或-COO- 基团,x和y表示1至15的整数,z表示0或1.该溶液或分散体,任选地在环酯聚合之后,在其制造过程结束时或之后混合到热塑性合成树脂中 处理阶段。

    Reacting olefins with ozone in a carboxylic acid medium
    6.
    发明授权
    Reacting olefins with ozone in a carboxylic acid medium 失效
    在羧酸介质中用臭氧反应烯烃

    公开(公告)号:US4287130A

    公开(公告)日:1981-09-01

    申请号:US191270

    申请日:1980-09-26

    CPC分类号: C07C51/34

    摘要: The process for reacting olefins with ozone in a carboxylic acid medium using pure oxygen or an oxygenated gas mixture for the ozone production, is improved by recycling the oxygen or the oxygenated gas mixture leaving the ozonizing stage.The oxygen containing gas leaving the ozonizing stage is:(a) washed with the carboxylic acid input of the ozonizing stage,(b) treated with an aqueous solution of an alkalinically reacting substance, and lastly,(c) dried and fed back to the ozonizer.

    摘要翻译: 使用纯氧或用于臭氧产生的氧化气体混合物在羧酸介质中使烯烃与臭氧反应的方法通过再循环离开臭氧化阶段的氧气或氧化气体混合物来改善。 离开臭氧化阶段的含氧气体是:(a)用臭氧化阶段的羧酸输入洗涤,(b)用碱性反应物质的水溶液处理,最后,(c)干燥并反馈至 臭氧发生器

    Process for the simultaneous manufacture of pure MTBE and a
substantially isobutene-free mixture of C.sub.4 -hydrocarbons
    7.
    发明授权
    Process for the simultaneous manufacture of pure MTBE and a substantially isobutene-free mixture of C.sub.4 -hydrocarbons 失效
    用于同时制造纯MTBE和基本上不含异丁烯的C 4烃混合物的方法

    公开(公告)号:US4282389A

    公开(公告)日:1981-08-04

    申请号:US100058

    申请日:1979-12-04

    CPC分类号: C07C41/06 C07C7/14891

    摘要: A process for the simultaneous manufacture of pure methyl tertiary butyl ether (MTBE) and a substantially isotubene-free mixture of C.sub.4 -hydrocarbons, by reacting the isobutene contained in the mixture of C.sub.4 -hydrocarbons with excess methanol in the liquid phase at elevated temperatures on strongly acid, macroporous, organic ion exchange resins.The process has the following steps:(a) methanol and isobutene are reacted in a molar ratio of 2:1 to 5:1 at temperatures between 30.degree. and 100.degree. C.;(b) the unconverted hydrocarbons are then removed as the top product under a pressure of 2 to 10 bars from a first rectification column;(c) the bottom product from this first column is rectified in a second column under normal pressure or under a slight excess pressure of up to 2 bars at the top of the column, the bottom product of this rectification is recycled to reaction zone (a), if necessary, after separating off a portion of the tertiary butanol formed and the C.sub.8 -olefins; and(d) the distillate from this second column is rectified in a third rectification column under a pressure of 5 to 30 bars, the distillate thus obtained is recycled into the feed to the second column and pure methyl tertiary butyl ether is withdrawn from the bottom of the third column.

    摘要翻译: 通过使C4-烃混合物中所含的异丁烯与过量的甲醇在液相中在高温下反应,同时制备纯甲基叔丁基醚(MTBE)和基本上不含异丁烯的C 4烃混合物的方法 强酸,大孔,有机离子交换树脂。 该方法具有以下步骤:(a)甲醇和异丁烯在30℃和100℃之间的温度下以2:1至5:1的摩尔比反应; (b)然后从第一精馏塔在2至10巴的压力下将未转化的烃作为顶部产物除去; (c)来自该第一塔的底部产物在常压或第二塔中在塔的顶部在常压或低至2巴的轻微过量压力下进行精馏,该精馏的底部产物再循环至反应区 ),如果需要,在分离一部分形成的叔丁醇和C8-烯烃之后; 和(d)来自该第二塔的馏出物在第三精馏塔中在5至30巴的压力下进行精馏,由此获得的馏出物再循环到进料到第二塔中,从底部排出纯甲基叔丁基醚 的第三列。

    Process for the preparation of copolymers useful as viscosity-raising
agents
    8.
    发明授权
    Process for the preparation of copolymers useful as viscosity-raising agents 失效
    制备可用作增粘剂的共聚物的方法

    公开(公告)号:US4212785A

    公开(公告)日:1980-07-15

    申请号:US937884

    申请日:1978-08-29

    申请人: Ulrich Turck

    发明人: Ulrich Turck

    摘要: In a process for the preparation of a viscosity raising copolymer, which comprises copolymerizing at an elevated temperature (a) methacrylic acid, (b) a conjugated diolefin, and (c) an ester of an .alpha.,.beta.-ethylenically unsaturated dicarboxylic acid, an improvement is provided wherein (a) 50-60% by weight of methacrylic acid, (b) 15-49% by weight of a conjugated diolefin, and (c) 1-25% by weight of fumaric acid dialkyl ester, maleic acid dialkyl ester or a mixture thereof, wherein each alkyl is of 1-8 carbon atoms, are copolymerized in an aqueous emulsion having a phase ratio of monomer mixture:water of 1:1.7 to 1:2.5, wherein, based on the monomer content, the aqueous phase contains 0.02-1% by weight of an alkaline compound, 0.05-1% by weight of an initiator, 0.01-1% by weight of a molecular weight regulator and 0.1-5% by weight of an emulsifier.

    摘要翻译: 在制备粘度提高共聚物的方法中,其包括在升高的温度(a)甲基丙烯酸,(b)共轭二烯烃和(c)α,β-烯键式不饱和二羧酸的酯, 提供改进,其中(a)50-60重量%的甲基丙烯酸,(b)15-49重量%的共轭二烯烃,和(c)1-25重量%的富马酸二烷基酯,马来酸二烷基酯 酯或其混合物,其中每个烷基为1-8个碳原子,在单体混合物:水的比例为1:1.7-1:2.5的水乳液中共聚合,其中基于单体含量, 水相含有0.02-1重量%的碱性化合物,0.05-1重量%的引发剂,0.01-1重量%的分子量调节剂和0.1-5重量%的乳化剂。

    Method of producing blocked polyisocyanates by reaction of an
imidazoline with an isocyanate
    9.
    发明授权
    Method of producing blocked polyisocyanates by reaction of an imidazoline with an isocyanate 失效
    通过咪唑啉与异氰酸酯的反应制备封端多异氰酸酯的方法

    公开(公告)号:US4200725A

    公开(公告)日:1980-04-29

    申请号:US921091

    申请日:1978-06-30

    IPC分类号: C07D233/06 C08G18/80

    CPC分类号: C07D233/06

    摘要: This invention relates to blocked isocyanates and to a method for making blocked isocyanates by blocking the isocyanate groups of a polyisocyanate, which may be chain extended, with a cyclic amidine compound of the formula ##STR1## where the R's are the same or different substituents inert to isocyanate groups.

    摘要翻译: 本发明涉及封闭的异氰酸酯和通过用式“IMAGE”的环状脒化合物封闭可延伸的多异氰酸酯的异氰酸酯基来制备封闭的异氰酸酯的方法,其中R是相同或不同的取代基惰性 到异氰酸酯基团。

    Process for preparing acetone from isobutyraldehyde
    10.
    发明授权
    Process for preparing acetone from isobutyraldehyde 失效
    从异丁醛制备丙酮的方法

    公开(公告)号:US4200589A

    公开(公告)日:1980-04-29

    申请号:US973579

    申请日:1978-12-27

    申请人: Helmut Scharf

    发明人: Helmut Scharf

    CPC分类号: C07C45/33

    摘要: This is an improvement in the process for preparing acetone by the catalytic, oxidative decarbonylation of isobutyraldehyde in the gaseous phase by passing a mixture consisting of isobutyraldehyde, oxygen and an inert diluent, when desired, at higher temperatures and at contact-times from 0.1 to 10 seconds over a carrier catalyst where the novel catalyst contains a mixture of copper oxide or manganese oxide, or a mixture thereof, with zinc oxide.A mixture comprising about 1 to 4.5 vol. % of isobutyraldehyde, about 1.2 to 99 vol. % of oxygen and an inert diluent, when desired, is passed over a catalyst at a temperature of about 130.degree. to 180.degree. C., consisting of about 0.1 to 6% by weight of Cu or Mn, or a mixture thereof, in the form of their oxides and of about 1 to 10% by weight of Zn in the form of zinc oxide on aluminum oxide as the carrier.

    摘要翻译: 这是通过在气相中通过异丁醛,氧气和惰性稀释剂组成的混合物在较高温度和接触时间从0.1至 其中新催化剂含有氧化铜或氧化锰或其混合物与氧化锌的混合物的载体催化剂上10秒钟。 包含约1至4.5体积% %的异丁醛,约1.2至99体积% 当需要时,氧气和惰性稀释剂的百分比在约130-180℃的温度下通过催化剂,由约0.1至6重量%的Cu或Mn或其混合物,在 形式的氧化物和约1至10重量%的氧化锌形式的氧化锌作为载体的Zn。