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    Pyrrolecarboxamides and pyrrolethioamides as fungicides
    12.
    发明授权
    Pyrrolecarboxamides and pyrrolethioamides as fungicides 失效
    吡咯酰胺和吡咯硫代酰胺作为杀真菌剂

    公开(公告)号：US07087638B2

    公开(公告)日：2006-08-08

    申请号：US10680346

    申请日：2003-10-07

    Applicant: Harald Walter ,  Hermann Schneider

    Inventor： Harald Walter ,  Hermann Schneider

    IPC: C07D409/12 ,  A01N43/10

    CPC classification number: C07D401/12 ,  A01N43/36 ,  A01N43/40 ,  A01N43/82 ,  C07D207/34 ,  C07D403/12 ,  C07D405/12 ,  C07D409/12 ,  C07D409/14 ,  C07D413/12 ,  C07D413/14 ,  C07D417/12 ,  C07D417/14

    Abstract: Novel pyrrole derivatives of formula I wherein X is oxygen or sulfur; R1 is C1–C4alkyl unsubstituted or substituted, with the exception of CF3; C3–C6cycloalkyl unsubstituted or substituted; or halogen; R2 is hydrogen, C1–C4alkyl unsubstituted or substituted, C1–C4alkoxy unsubstituted or substituted, cyano or halogen; R3 is C1–C4alkyl unsubstituted or substituted; and A is orthosubstituted aryl; orthosubstituted heteroaryl; bicycloaryl unsubstituted or substituted; or bicycloheteroaryl unsubstituted or substituted. The novel compounds have plant-protective properties and are suitable for protecting plants against infestations by phytopathogenic microorganisms.

    Abstract translation: 式I的新型吡咯衍生物，其中X是氧或硫; R 1是未取代或取代的C 1 -C 4烷基，但CF 3 3除外。 未取代或取代的C 3 -C 6环烷基; 或卤素; R 2是氢，未取代或取代的C 1 -C 4烷基，C 1 -C 3 - 4个未取代的或取代的，氰基或卤素的烷氧基; R 3是未取代或取代的C 1 -C 4烷基; 和A是邻位取代的芳基; 邻位取代的杂芳基; 未取代或取代的双环芳基; 或双环杂芳基未取代或取代。 新化合物具有植物保护性质，适用于通过植物病原微生物保护植物免受侵袭。

    Process for controlling a closing device in a motor vehicle
    13.
    发明授权
    Process for controlling a closing device in a motor vehicle 有权
    用于控制机动车辆中的关闭装置的过程

    公开(公告)号：US07000982B2

    公开(公告)日：2006-02-21

    申请号：US10821205

    申请日：2004-04-09

    Applicant: Steffen Kreiner ,  Hermann Schneider

    Inventor： Steffen Kreiner ,  Hermann Schneider

    IPC: B60J7/057

    CPC classification number: B60J7/0573

    Abstract: In a process for controlling a closing device in a motor vehicle driven by an electric motor, in particular for controlling a motor vehicle sunroof, to protect a body part from being crushed during a closing motion, a closing resistance variable is detected. The closing resistance variable is characteristic of a force counteracting the closing motion, and is used to determine whether a crush situation exists. For this purpose, an additional auxiliary variable indicative of wind load forces at a certain speed is used. If a crush situation exists, a protective measure is initiated.

    Abstract translation: 在用于控制由电动机驱动的机动车辆中的关闭装置的过程中，特别是用于控制机动车辆天窗的过程中，为了保护身体部分在关闭运动期间不被压碎，检测到闭合阻力变量。 闭合阻力变量是抵消闭合运动的力的特征，并且用于确定是否存在挤压情况。 为此，使用了以一定速度表示风荷载力的附加辅助变量。 如果存在压倒性的情况，则开始采取保护措施。

    Process for determining and evaluating the combustion pressure of an internal combustion engine
    14.
    发明授权
    Process for determining and evaluating the combustion pressure of an internal combustion engine 失效
    用于确定和评估内燃机的燃烧压力的方法

    公开(公告)号：US5020360A

    公开(公告)日：1991-06-04

    申请号：US477981

    申请日：1990-04-27

    Applicant: Thomas Brosi ,  Werner Hess ,  Winfried Moser ,  Hermann Schneider

    Inventor： Thomas Brosi ,  Werner Hess ,  Winfried Moser ,  Hermann Schneider

    IPC: G01L23/00 ,  F02B1/04 ,  F02D35/02 ,  F02D41/38 ,  F02D41/40 ,  F02D45/00 ,  G01M15/00 ,  G01M15/04 ,  G01M15/08

    CPC classification number: F02D41/38 ,  F02D35/023 ,  F02D35/028 ,  F02D41/401 ,  F02P5/153 ,  G01M15/08 ,  F02B1/04 ,  F02D2041/286 ,  F02D35/024 ,  Y02T10/44 ,  Y02T10/46

    Abstract: A process for determining the combustion pressure of an internal combustion engine is proposed. Conventional processes of this type have the disadvantage that the determination methods are very costly. Furthermore, stringent requirements are made of the sensors to be used. By comparison, the process proposed here is distinguished in that the combustion pressure is calculated from the combustion chamber pressure (p(.alpha.)) determined with simple sensors, by determining the compression pressure (p.sub.k (.alpha.)). These values for the compression pressure are subtracted from the combustion chamber pressure in order to calculate the combustion pressure p*(.alpha.)). Preferably, the course of the compression pressure is obtained by measuring the combustion chamber pressure values during the compression until top dead center in the working phase and storing them in a memory. The compression values occurring after top dead center are obtained by reflection at an axis extending through top dead center, resulting in a symmetrical curve course for the compression pressure. In this way, the combustion pressure can be calculated particularly simply.

    Abstract translation: PCT No.PCT / DE88 / 00657 Sec。 371日期1990年04月27日第 102（e）日期1990年4月27日PCT提交1988年10月26日PCT公布。 WO89 / 03983 PCT出版物 日期：1989年5月5日。提出了一种用于确定内燃机的燃烧压力的方法。 这种常规方法的缺点是确定方法非常昂贵。 此外，要使用的传感器要求严格。 相比之下，这里提出的方法的区别在于，通过确定压缩压力（pk（α）），从由简单传感器确定的燃烧室压力（p（α））计算燃烧压力。 为了计算燃烧压力p *（α），从燃烧室压力中减去压缩压力的这些值。 优选地，压缩压力的过程通过在压缩期间测量燃烧室压力值直到工作阶段的上止点并将其存储在存储器中来获得。 通过在延伸穿过上止点的轴上的反射获得在上止点之后发生的压缩值，导致压缩压力的对称曲线。 以这种方式，可以特别简单地计算燃烧压力。

    Preparation of N-thienyl-chloroacetamides and tetrahydro-thien-3-ylidenimines
    15.
    发明授权
    Preparation of N-thienyl-chloroacetamides and tetrahydro-thien-3-ylidenimines 失效
    N-噻吩基 - 氯乙酰胺和四氢 - 噻吩-3-亚基亚胺的制备

    公开(公告)号：US4806656A

    公开(公告)日：1989-02-21

    申请号：US762333

    申请日：1985-08-05

    Applicant: Hermann Schneider

    Inventor： Hermann Schneider

    IPC: C07D333/32 ,  C07D333/36 ,  C07D333/42 ,  C25C1/12

    CPC classification number: C25C1/12 ,  C07C323/00 ,  C07D333/32 ,  C07D333/36

    Abstract: The invention provides compounds of formula I ##STR1## wherein R is C.sub.1-4 alkoxy-C.sub.2-4 alkyl of which the C.sub.1-4 alkoxy group is separated by at least 2 C-atoms from the N-atom to which R is bound,each of R.sub.2 and R.sub.4 independently is CH.sub.3 or C.sub.2 H.sub.5 andR.sub.5 is H or CH.sub.3,the preparation of such compounds and the use of such compounds for the preparation of N-(thien-3-yl)-chloroacetamides.

    Abstract translation: 本发明提供式I化合物其中R为C 1-4烷氧基-C 2-4烷基，其中C 1-4烷氧基与R所结合的N-原子分开至少2个C原子， R2和R4独立地是CH3或C2H5，R5是H或CH3，这些化合物的制备以及这些化合物用于制备N-（噻吩-3-基） - 氯乙酰胺的用途。

    Process for the direct reduction of iron-oxide-containing materials
    16.
    发明授权
    Process for the direct reduction of iron-oxide-containing materials 失效
    直接还原含氧化铁材料的方法

    公开(公告)号：US4729786A

    公开(公告)日：1988-03-08

    申请号：US760943

    申请日：1985-07-31

    Applicant: Hermann Schneider ,  Konstantin Milionis ,  Hermann Pusch

    Inventor： Hermann Schneider ,  Konstantin Milionis ,  Hermann Pusch

    IPC: C21B13/00 ,  C21B13/02

    CPC classification number: C21B13/02 ,  Y02P10/122 ,  Y02P10/126 ,  Y02P10/128 ,  Y02P10/136

    Abstract: There is disclosed a process for the direct reduction of iron-oxide-containing materials by a gasification gas produced in a gasifier by reacting carbon with oxygen and, if desired, with steam, upon the addition of sulfur acceptors in a fluidized bed. The gasification gas is supplied to a direct reduction shaft furnace after separation of solid particles carried therewith. At least part of the top gas withdrawn from the direct reduction shaft furnace is compressed after dust scrubbing and is recycled to the gasifier. The sulfur acceptors are supplied as fine particles separated from the coal in cocurrent with, and/or counterflow to, the fluidized-bed forming gases. The top gas from the reduction shaft furnace, which has a concentration of from 15 to 30% CO.sub.2 and a temperature of from 80.degree. to 800.degree. C., is recycled laterally through the wall of the gasifier into the region of the fluidized bed, which is maintained at a temperature of at least 1,150.degree. C. The slag, which is in the molten state with the temperature prevailing in the gasifier, containing ashes and sulfur compounds and collecting under the formation of a bath, is removed via a tap in the vicinity of the bottom of the gasifier. The solid particles separated from the gasification gas are mixed with dust coal having a grain size of up to 3 mm and are recycled into the bottom region of the gasifier above the surface of the slag bath.

    Abstract translation: 公开了一种通过在气化器中产生的气化气体直接还原含氧化铁材料的方法，所述气化气体在流化床中加入硫受体时，使碳与氧气反应，如果需要，通过蒸汽反应。 在分离固体颗粒后，将气化气体供给到直接还原炉。 从直接还原竖炉中排出的顶部气体的至少一部分在除尘后被压缩并被再循环到气化器。 硫受体以与流化床形成气体并流和/或逆流的方式与煤分离的细颗粒供应。 来自还原竖炉的顶部气体，其浓度为15-30％CO 2，温度为80-800℃，通过气化器壁横向回收到流化床的区域中， 其保持在至少1150℃的温度。在气化器中具有含有灰分和硫化合物并在浴形成下收集的处于熔融状态的炉渣通过水龙头去除 气化炉底部附近。 与气化气体分离的固体颗粒与颗粒尺寸高达3mm的粉煤混合，并再循环到炉渣表面上方的气化器的底部区域。

    Process for the preparation of bicyclic diketone salts
    19.
    发明授权
    Process for the preparation of bicyclic diketone salts 失效
    双环二酮盐的制备方法

    公开(公告)号：US06911547B1

    公开(公告)日：2005-06-28

    申请号：US10408950

    申请日：2003-04-08

    Applicant: Hermann Schneider ,  Christoph Lüthy

    Inventor： Hermann Schneider ,  Christoph Lüthy

    IPC: C07D311/94 ,  C07B61/00 ,  C07C45/51 ,  C07C45/57 ,  C07C45/60 ,  C07C49/443 ,  C07C49/733 ,  C07D311/00 ,  C07D313/06 ,  C07D313/08 ,  C07D313/02 ,  C07C45/27

    CPC classification number: C07D311/00 ,  C07C45/511 ,  C07C45/57 ,  C07C45/60 ,  C07C49/443 ,  C07C49/733 ,  C07D313/06 ,  Y02P20/582

    Abstract: The present invention relates to a process for the preparation of bicyclic 1,3-diketone salts of formula I wherein R1, R2, R3 and R4 are each independently of the others hydrogen or C1-C4alkyl; A and E are each independently of the other C1-C2alkylene, which may be substituted once or up to four times by a C1-C4alkyl group, and M+is an alkali metal ion, alkaline earth metal ion or ammonium ion, by oxidation of a compound of formula II to a compound of formula III and subsequent conversion to a compound of formula I either in the presence of a base and a catalytic amount of a cyanide or in the presence of an alkali metal alcoholate or alkaline earth metal alcoholate, and to novel bicyclic enol lactone intermediates of formula III for use in that process.

    Abstract translation: 本发明涉及一种制备式I的双环1,3-二酮盐的方法，其中R 1，R 2，R 3， >和R 4各自独立地为氢或C 1 -C 4烷基; A和E各自独立于另一个C 1 -C 2亚烷基，其可以被C 1〜N取代一次或多达四次 > -C 4烷基，M + S是碱金属离子，碱土金属离子或铵离子，通过将式II化合物氧化成式 式III化合物，随后在碱和催化量的氰化物的存在下或在碱金属醇盐或碱土金属醇化物的存在下转化为式I化合物，以及式III的新型双环烯醇内酯中间体 用于该过程。

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