PROJECTION OPTICAL SYSTEM, PROJECTOR AND IMAGE READING DEVICE
    1.
    发明申请
    PROJECTION OPTICAL SYSTEM, PROJECTOR AND IMAGE READING DEVICE 有权
    投影光学系统,投影仪和图像读取装置

    公开(公告)号:US20100097582A1

    公开(公告)日:2010-04-22

    申请号:US12529920

    申请日:2008-03-05

    IPC分类号: G03B21/28

    CPC分类号: G03B21/28 G02B17/0804

    摘要: A projection optical system which has a short total length but can project a high quality and large image. The projection optical system projects the displayed image on an image displaying surface onto a projection surface, and includes a lens system having a plurality of lenses, and one or more curved mirrors. Light flux of an enlarged image shooting out from the lens system to the projection surface is incident onto a mirror surface of the one of the curved mirrors first of all. A distance OAL and a distance Y satisfy a requirement (1) 20

    摘要翻译: 一种投影光学系统,其总长度短,但可投影高品质和大图像。 投影光学系统将显示的图像投影到图像显示表面到投影表面上,并且包括具有多个透镜的透镜系统和一个或多个曲面镜。 从透镜系统向投影面射出的放大图像的光通量首先入射到一个曲面镜的镜面上。 距离OAL和距离Y满足要求(1)20

    Projection optical system, projector and image reading device
    2.
    发明授权
    Projection optical system, projector and image reading device 有权
    投影光学系统,投影仪和图像读取装置

    公开(公告)号:US08419191B2

    公开(公告)日:2013-04-16

    申请号:US12529920

    申请日:2008-03-05

    IPC分类号: G03B21/22 G03B21/28 G02B17/00

    CPC分类号: G03B21/28 G02B17/0804

    摘要: An optical system with short total length to project a high quality large image. The system projects an image onto a projection surface, and includes a lens system having a plurality of lenses, and one or more curved mirrors. Light flux of an enlarged image shooting out from the lens system to the projection surface is incident onto a mirror surface of the one of the curved mirrors first of all. Distances OAL and Y satisfy a requirement 20

    摘要翻译: 总体长度短的光学系统投射高质量的大图像。 系统将图像投影到投影表面上,并且包括具有多个透镜的透镜系统和一个或多个曲面镜。 从透镜系统向投影面射出的放大图像的光通量首先入射到一个曲面镜的镜面上。 距离OAL和Y满足要求20

    Process for preparing high-purity aniline
    3.
    发明授权
    Process for preparing high-purity aniline 失效
    制备高纯度苯胺的方法

    公开(公告)号:US5616806A

    公开(公告)日:1997-04-01

    申请号:US760771

    申请日:1991-09-17

    CPC分类号: C07C209/36

    摘要: A process for the continuous preparation of aniline by hydrogenating nitrobenzene with hydrogen is disclosed which comprises the steps of suspending, in an aniline solvent, a catalyst of palladium or palladium-platinum which is deposited on a lipophilic carbon having an oil absorbency of at least 100, and carrying out reaction at a temperature of from 150.degree. to 250.degree. C. substantially in the absence of water while aniline and water formed in said reaction are continuously distilled off as vapor from the reaction product, and the concentration of nitrobenzene in the reaction solution is maintained at 0.01% by weight or less, wherein a zinc compound is added to the reaction system as a promotor and carbon monoxide is added to the hydrogen at a concentration of 1-500 ppm.

    摘要翻译: 公开了通过用氢气氢化硝基苯连续制备苯胺的方法,该方法包括以下步骤:在苯胺溶剂中悬浮钯或钯 - 铂的催化剂,所述催化剂沉积在具有至少100的吸油性的亲脂性碳上 并且在150-250℃的温度下进行反应,基本上不存在水,而在反应中形成的苯胺和水作为蒸气从反应产物中连续蒸馏出去,反应中硝基苯的浓度 溶液维持在0.01重量%以下,其中将锌化合物作为促进剂加入反应体系中,一氧化碳以1-500ppm的浓度加入到氢气中。

    Production process of chlorine
    6.
    发明授权
    Production process of chlorine 失效
    氯的生产过程

    公开(公告)号:US4803065A

    公开(公告)日:1989-02-07

    申请号:US64699

    申请日:1987-06-22

    CPC分类号: B01J23/26 C01B7/04 Y02P20/228

    摘要: An improved process is provided for the production of chlorine. In a fluidized-bed reactor having a specific equivalent diameter and made of a material with a particular iron content, hydrogen chloride and oxygen are reacted in particular gas volumes and at specific molar ratio, superficial velocity, temperature and pressure in the presence of a catalyst composed principally of a chromium oxide and having a specific particle size distribution. The catalyst is filled in a specific amount in terms of catalyst layer height at rest. The catalyst can retain its high activity.

    摘要翻译: 提供了一种用于生产氯的改进方法。 在具有特定当量直径并由具有特定铁含量的材料制成的流化床反应器中,氯化氢和氧气在特定的气体体积下以特定的摩尔比在表面速度,温度和压力下在催化剂存在下反应 主要由氧化铬组成并具有特定的粒度分布。 以催化剂层的静置高度,催化剂以特定的量填充。 催化剂可以保持其高活性。

    Industrial process for the separation and recovery of chlorine
    8.
    发明授权
    Industrial process for the separation and recovery of chlorine 失效
    用于分离和回收氯的工业过程

    公开(公告)号:US5254323A

    公开(公告)日:1993-10-19

    申请号:US921606

    申请日:1992-08-03

    IPC分类号: C01B7/07 C01B7/01 B01D53/34

    CPC分类号: C01B7/0743

    摘要: A gaseous mixture containing chlorine, carbon dioxide and non-condensable gas is compressed and cooled to separate it into a residual gas formed principally of a major portion of the non-condensable gas and a condensate formed primarily of chlorine. The condensate is fed to a stripping column to desorb carbon dioxide and a minor portion of the non-condensable gas dissolved in the condensate. The stripped gas formed primarily of chlorine and carbon dioxide may be treated further. Namely, the stripped gas is mixed with the residual gas. At least a portion of the mixed gas is fed into an absorption column, whereby a major portion of remaining chlorine is absorbed to lower the chlorine content Removal of chlorine from such a gaseous mixture or an off-gas from the above process can be achieved by washing it with an aqueous solution or suspension containing an alkali metal sulfite and/or an alkaline earth metal sulfite while controlling the pH of the solution or suspension within a range of 1.9-6.3.

    摘要翻译: 将含有氯,二氧化碳和不可冷凝气体的气体混合物压缩并冷却,将其分离成主要由不可冷凝气体主要形成的残留气体和主要由氯气形成的冷凝物。 将冷凝物供入汽提塔以解吸二氧化碳和少部分溶解在冷凝物中的不可冷凝气体。 主要由氯和二氧化碳形成的汽提气体可以进一步处理。 即,将汽提的气体与残留气体混合。 将混合气体的至少一部分进料到吸收塔中,从而吸收主要部分的剩余氯以降低氯含量从上述方法从这种气体混合物或废气中除去氯可以通过 用包含碱金属亚硫酸盐和/或碱土金属亚硫酸盐的水溶液或悬浮液洗涤,同时将溶液或悬浮液的pH控制在1.9-6.3的范围内。

    Industrial process for the separation and recovery of chlorine
    9.
    发明授权
    Industrial process for the separation and recovery of chlorine 失效
    用于分离和回收氯的工业过程

    公开(公告)号:US5000006A

    公开(公告)日:1991-03-19

    申请号:US310929

    申请日:1989-02-16

    IPC分类号: C01B7/01 B01D53/68 C01B7/07

    摘要: A gaseous mixture containing chlorine, carbon dioxide and non-condensable gas is compressed and cooled to separate it into a residual gas formed principally of a major portion of the non-condensable gas and a condensate formed primarily of chlorine. The condensate is fed to a stripping column to desorb carbon dioxide and a minor portion of the non-condensable gas dissolved in the condensate. The stripped gas formed primarily of chlorine and carbon dioxide may be treated further. Namely, the stripped gas is mixed with the residual gas. At least a portion of the mixed gas is fed into an absorption column, whereby a major portion of remaining chlorine is absorbed to lower the chlorine content. Removal of chlorine from such a gaseous mixture or an off-gas from the above process can be achieved by washing it with an aqueous solution or suspension containing an alkali metal sulfite and/or an alkaline earth metal sulfite while controlling the pH of the solution or suspension within a range of 1.9-6.3.