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    • 1. 发明申请
    • ORGANIC OPTICAL COMPONENTS AND PREPARATION THEREOF
    • 有机光学元件及其制备
    • WO1995009726A1
    • 1995-04-13
    • PCT/GB1994002118
    • 1994-09-29
    • IMPERIAL CHEMICAL INDUSTRIES PLCSUMMERSGILL, PhilipHARVEY, Thomas, GriersonRYAN, Timothy, GeorgeCARTER, NeilTHORNE, Andrew, John
    • IMPERIAL CHEMICAL INDUSTRIES PLC
    • B29D11/00
    • B32B7/02B29C43/28B29D11/0073B29K2105/24B32B27/08B32B37/1284B32B2038/0076B32B2307/418B32B2551/00
    • A polymeric structure for use in the preparation of an organic optical component which polymeric structure comprises (a) a first layer (2) of an optically transmissive first polymer having a first refractive index, the first layer having a surface in which is defined at least one retaining feature (3); (b) an optically transmissive second polymer retained within the at least one retaining feature, the second polymer having a second refractive index which is greater than the first refractive index; and (c) an overlay of the second polymer having a maximum thickness of less than 1.5 mu m over the surface of the first layer. An organic optical component prepared from such a structure shows an optical loss of less than 2.0 dB.cm-1 at at least one wavelength in the range 300 to 1600 nm. The method of forming such a structure, e.g. waveguide, requires forming a line of contact between a flexible dispensing layer and the polymer surface in which the features defining the waveguide are located and progressively contacting the surface with the flexible dispensing layer such the line of contact advances across the surface. Sufficient of a resin (6) capable of forming the second polymer is applied along the line of contact and sufficient pressure is applied such that substantially all of the resin which is surplus to that required to fill the feature progresses with the line of contact.
    • 一种用于制备有机光学部件的聚合物结构,所述聚合物结构包括(a)具有第一折射率的光学透射的第一聚合物的第一层(2),所述第一层的表面至少被限定在其中 一个保留特征(3); (b)保留在所述至少一个保留特征内的光学透射的第二聚合物,所述第二聚合物具有大于所述第一折射率的第二折射率; 和(c)在第一层的表面上具有小于1.5μm的最大厚度的第二聚合物的覆盖层。 由这种结构制备的有机光学部件在300〜1600nm的范围内的至少一个波长的光损失小于2.0dB·cm -1。 形成这种结构的方法,例如 波导管需要在柔性分配层与聚合物表面之间形成接触线,其中限定波导的特征位于该表面,并且使柔性分配层逐渐接触表面,使得该接触线穿过该表面。 沿着接触线施加足够的能够形成第二聚合物的树脂(6),并且施加足够的压力,使得基本上所有满足填充特征所需要的剩余的树脂随着接触线进行。
    • 4. 发明申请
    • PROCESS FOR REMOVING CHLORINE FROM GAS STREAM
    • 从气体流中除去氯化物的方法
    • WO1998025689A1
    • 1998-06-18
    • PCT/GB1997003175
    • 1997-11-19
    • IMPERIAL CHEMICAL INDUSTRIES PLCSTITT, Edmund, HughHANCOCK, Frederick, Ernest
    • IMPERIAL CHEMICAL INDUSTRIES PLC
    • B01D53/68
    • B01D53/1425B01D53/68
    • Chlorine is scrubbed from a chlorine-containing gas using an aqueous feed liquor containing an excess of alkali to give an effluent liquor containing chloride and hypochlorite ions. The effluent liquor is recycled as part or all of the aqueous feed liquor. For at least part of the time, at least part of the effluent liquor is passed through a fixed bed of a catalyst for the decomposition of hypochlorite ions whereby hypochlorite ions are decomposed to oxygen gas and chloride ions. The resultant catalyst-treated liquor is mixed with the remainder, if any, of the effluent liquor and recycled, optionally together with added fresh alkali solution, as the aqueous feed liquor. Part of the effluent liquor is optionally discharged as a purge stream before or after passage through catalyst bed. The process may be operated in a continuous mode or in a semi-continuous mode wherein a reservoir holding the liquor to be recycled is periodically discharged, preferably through the catalyst bed, and then recharged with fresh alkali solution. Altternatively two reservoirs may be employed with one supplying the aqueous feed liquor while the other is being discharged and replenished. In the latter case, the reservoir being discharged may have its liquor discharged through the catalyst bed.
    • 使用含有过量碱的含水原料液从含氯气体中洗涤氯,得到含有氯化物和次氯酸根离子的废液。 流出液被回收作为部分或全部含水进料液。 在至少部分时间内,至少部分废液通过催化剂的固定床,以分解次氯酸根离子,从而将次氯酸根离子分解成氧气和氯离子。 将得到的催化剂处理的液体与其余的(如果有的话)的流出液混合,并且任选地与添加的新鲜碱溶液一起再循环,作为含水进料液。 在通过催化剂床之前或之后,部分流出液可任选地作为吹扫流排出。 该方法可以以连续模式或半连续模式操作,其中保持待循环液体的储存器周期性排出,优选通过催化剂床排出,然后用新鲜碱溶液再充电。 或者,可以使用两个储存器,一个供应水性进料液,另一个被排出并补充。 在后一种情况下,被排出的储存器可以使其液体通过催化剂床排出。