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    专

    基于标识的强权限控制模式下联盟链身份认证方式

    KR8139096B1
    发明人
    邱望洁
    受让人
    UNIV BEIHANG
    申请人
    IGARASHI AKIRA, MATSUSHITA ELECTRIC WORKS LTD
    申请号
    18520776
    申请日
    2018-03-28
    公开(公告)号
    KR8139096B1
    公开(公告)日
    1974-07-31
    IPC分类号
    F24C005/20F24C015/00
    CPC分类号
    -
    优先权号
    199718
    80002620
    11026891
    2995434
    706278
    优先权日
    2015-12-13
    2017-03-09
    2017-12-12
    2018-02-11
    2018-03-04
    摘要

    NOVELTY - Structure of a hood lock lower reinforcement is provided to prevent the degradation of stiffness due to the thermal degradation by dispersing an external load to a round bar added to the rear face of a welding portion.

    DETAILED DESCRIPTION - A round bar(10) is fixed to the rear portion of a welding portion by tack welding(11). Since the round bar is fixed by tack welding, thermal degradation is avoided. A load is dispersed by reinforcing a weak portion formed due to thermal degradation by welding.

    权利要求
    1.一种音频的高频优化方法,其特征在于,包括: 对获取到的低采样率音频进行高频重建,得到高采样率音频; 根据所述低采样率音频和高采样率音频分别计算得到低采样率频域信号和高采样率频域信号; 判断所述低采样率频域信号与高采样率频域信号的低频差异是否满足预设条件;所述预设条件为所述低频差异大于预设阈值; 若是,则根据低采样率频域信号对高采样率频域信号的低频进行替换处理,且对高采样率频域信号的高频进行第一次平滑处理; 若否,则对高采样率频域信号的高频进行第一次平滑处理; 对低采样率频域信号进行基频搜索,判断是否存在基频; 若是,则根据基频对第一次平滑处理后的高采样率频域信号的高频进行第二次平滑处理。
    2.如权利要求1所述的音频的高频优化方法,其特征在于,所述判断所述低采样率频域信号与高采样率频域信号的低频差异是否满足预设条件,具体包括: 根据公式 计算比值D;其中,FN[i]为低采样率频域信号中每一帧的第i个频点,FM[i]为高采样率频域信号中每一帧的第i个频点;LN为低采样率频域信号中每一帧的频点数; 判断比值D是否大于预设阈值。
    3.如权利要求1所述的音频的高频优化方法,其特征在于,所述对高采样率频域信号的高频进行第一次平滑处理,具体包括: 根据公式FM t [i]=a·FM t [i]+a 2 ·FM t-1 [i]+a 3 ·FM t-2 [i]+…+a n+1 ·FM t-n [i]对高采样率频域信号的高频进行第一次平滑处理;其中,FM t [i]为高采样率频域信号的当前帧t的第i个频点,FM t-n [i]为高采样率频域信号的第(t-n)帧的第i个频点;i∈[LN+1,LM],LN为低采样率频域信号中每一帧的频点数,LM为高采样率频域信号中每一帧的频点数,a为预设的第一平滑因子。
    4.如权利要求1所述的音频的高频优化方法,其特征在于,所述根据基频对第一次平滑处理后的高采样率频域信号的高频进行第二次平滑处理,具体包括: 根据公式 对第一次平滑处理后的高采样率频域信号的高频进行第二次平滑处理;其中,f 0 表示基频, f 0 ∈[0,LN],FM[f k ]为第一次平滑处理后的高采样率频域信号中每一帧的第f k 个频点,f k ∈[LN+1,LM],FM[f k +i]为第一次平滑处理后的高采样率频域信号中每一帧的第(f k +i)个频点,LN为低采样率频域信号中每一帧的频点数,LM为高采样率频域信号中每一帧的频点数,b为预设的第二平滑因子。
    5.如权利要求1所述的音频的高频优化方法,其特征在于,还包括:根据平滑处理后的高采样率频域信号,计算得到高采样率时域信号。
    6.如权利要求1所述的音频的高频优化方法,其特征在于,所述对获取到的低采样率音频进行高频重建,得到高采样率音频,具体包括: 对获取到的低采样率音频进行特征提取,得到特征向量; 根据预先训练好的机器学习模型计算得到与所述特征向量欧式距离最小的数据组,所述数据组中的高采样率数据即为所述高采样率音频。
    7.如权利要求1所述的音频的高频优化方法,其特征在于,所述对获取到的低采样率音频进行高频重建,得到高采样率音频,具体包括: 将获取到的低采样率音频输入预先训练好的深度学习网络中,得到所述高采样率音频。
    8.一种音频的高频优化装置,其特征在于,包括: 高采样率音频获得模块,用于对获取到的低采样率音频进行高频重建,得到高采样率音频; 频域信号计算模块,用于根据所述低采样率音频和高采样率音频分别计算得到低采样率频域信号和高采样率频域信号; 预设条件判断模块,用于判断所述低采样率频域信号与高采样率频域信号的低频差异是否满足预设条件;所述预设条件为所述低频差异大于预设阈值; 第一处理模块,用于当所述低采样率频域信号与高采样率频域信号的低频差异满足预设条件时,根据低采样率频域信号对高采样率频域信号的低频进行替换处理,且对高采样率频域信号的高频进行第一次平滑处理;当所述低采样率频域信号与高采样率频域信号的低频差异不满足预设条件时,则对高采样率频域信号的高频进行第一次平滑处理; 基频判断模块,用于对低采样率频域信号进行基频搜索,判断是否存在基频; 第二处理模块,用于当判断存在基频时,根据基频对第一次平滑处理后的高采样率频域信号的高频进行第二次平滑处理。
    9.一种音频的高频优化装置,其特征在于,包括处理器、存储器以及存储在所述存储器中且被配置为由所述处理器执行的计算机程序,所述处理器执行所述计算机程序时实现如权利要求1至7中任意一项所述的音频的高频优化方法。
    10.一种计算机可读存储介质,其特征在于,所述计算机可读存储介质包括存储的计算机程序,其中,在所述计算机程序运行时控制所述计算机可读存储介质所在设备执行如权利要求1至7中任意一项所述的音频的高频优化方法。
    说明书
    [0001]This application is a 371 of International Application No, PCT/EP2005/002230 filed Mar. 3, 2005, which claims priority to GB 0406894,6 filed Mar. 26, 2004, the contents of which are incorporated herein by reference.
    [0002]The present invention relates to a novel method for reducing the cyanide content of a mesotrione sample.
    [0003]Mesotrione (2-(2′-nitro-4′-methylsulphonyl benzoyl)-1,3-cyclohexanedione) is a selective corn herbicide and has the structure of formula (I)
    [0004]Mesotrione is prepared by reacting 2-nitro-4-methylsulphonyl benzoyl chloride with cyclohexanedione to give the enol ester, followed by a rearrangement reaction to give mesotrione, as shown in the following reaction scheme:
    [0005]2-Nitro-4-methylsulphonyl benzoyl chloride is prepared from the corresponding benzoic acid, which in turn is prepared by oxidation of 2-nitro-4-methylsulphonyl toluene. More details on the preparative route may be found in U.S. Pat. No. 4,695,673.
    [0006]During the rearrangement process, the mesotrione sample is contaminated with cyanide residues from the acetone cyanohydrin catalyst. It is therefore an object of the present invention to provide a simple, but effective method for reducing the level of cyanide residues in the mesotrione sample to an acceptable level.
    [0007]It has surprisingly been found that adjusting the pH of a mesotrione sample in aqueous solution has a significant impact on the resulting cyanide levels.
    [0008]Accordingly the present invention provides a method for reducing the cyanide levels in a mesotrione sample, said method comprising:
    [0009](i) taking an aqueous solution of the mesotrione sample in an aqueous solvent,
    [0010](ii) adjusting the pH of said aqueous solution to a value of 9.5 or higher, and
    [0011](iii) crystallising the mesotrione out of solution.
    [0012]In one embodiment of the invention, the mesotrione sample has previously been isolated, and the aqueous solution is formed by dissolving the isolated sample in an aqueous solvent.
    [0013]In a second embodiment of the invention, the mesotrione sample has not previously been isolated and remains dissolved in the aqueous solvent used in the condensation/rearrangement reaction described above.
    [0014]The aqueous solvent may be selected from the group consisting of water and a water soluble solvent, such as acetonitrile, triethylamine, methanol, ethanol, acetone. Preferably, the aqueous solvent is water. The mesotrione sample is suitably dissolved in the aqueous solvent to give a solution concentration of from 1% to 30%, suitably from 5% to 15%, and preferably from 8% to 11%.
    [0015]Suitably, the pH of the aqueous solution is raised to a pH of at least 11, and preferably at least 11.5. Suitably, the aqueous mesotrione sample is held at a pH of at least 9.5 for at least 5 minutes, suitably at least 15 minutes and preferably at least 30 minutes.
    [0016]Suitably, the temperature of the aqueous solution should not be greater than 30° C.
    [0017]The crystallisation is carried out according to standard laboratory procedures. For example, for a batch crystallisation, the final pH is adjusted from its starting value of 9.5 or higher to pH 2.5 by charging hydrochloric acid to the crystalliser. The hydrochloric acid should be charged in a manner to ensure adequate mixing. The crystallisation process may also be carried out as a semi-batch or continuous process. The crystallisation step may also include a nitrogen-sparging step, wherein nitrogen is bubbled through the crystallisation vessel in a continuous fashion and sent to a scrubber.
    [0018]The method of the invention may further include a distillation step to remove solvents when the mesotrione sample has not previously been isolated (i.e. the second embodiment of the invention). The distillation step may be carried out either before or after adjusting the pH to 9.5 or higher. The distillation step is suitably carried out using a sufficient amount of steam to remove the solvents from the aqueous solution.
    [0019]Suitably, the method of the invention reduces the cyanide levels in the mesotrione sample to 150 ppm or less, more suitably 100 ppm or less and preferably 50 ppm or less.
    [0020]The invention will now be described further with reference to the following examples, which are illustrative but not limiting of the invention.
    [0021]EXAMPLE 1
    [0022]Wet paste mesotrione that was high in total CN was subjected to different treatments in an effort to reduce the total CN content. The results are shown in Table 1.
    [0023]TABLE 1 Cyanide Original Content % Cyanide after reduction Example Content Treatment in Cyanide No. Treatment (PPM) (PPM) content 1A Mesotrione was placed in water to make 546 15 97% an aqueous solution at a concentration of ~10%, pH was adjusted to >13, ACN was charged, and the mixture was then batch crystallised following standard lab procedures. 1B Mesotrione was placed in water to make 1114 557 50% an aqueous solution at a concentration of ~10%, pH was adjusted to 11.3, ACN was charged, and the mixture was batch crystallised following standard lab procedures. 1C Mesotrione was placed in water to make 1114 50 96% an aqueous solution at a concentration of ~10%, pH was adjusted to >13, ACN was charged, and the mixture was batch crystallised following standard lab procedures. 1D Mesotrione was placed in water to make 690 150 78% an aqueous solution at a concentration of ~10%, pH was adjusted to 11.3, ACN was charged, and the mixture was batch crystallised following standard lab procedures. 1E Mesotrione was placed in water to make 690 170 75% an aqueous solution at a concentration of ~10%, pH was adjusted to 12-13, ACN was charged, and the mixture was batch crystallised following standard lab procedures.
    [0024]EXAMPLE 2
    [0025]Mesotrione was crystallised from samples taken from the plant during the solvent distillation. Samples were taken from the same batch after both 4500 lbs steam (distillation not finished) and 5000 lbs steam (distillation finished) had been used during the distillation process. The pH of the sample was adjusted and the samples were crystallised via standard lab procedures. Total CN content was measured by titration of the wet paste. The results are given in Table 2.
    [0026]TABLE 2 Example Distillation Starting pH of Total CN of wet No. Complete? crystallisation paste (PPM) 2A No 9.5 278 2B Yes 9.5 651 2C No 11.1 120 2D Yes 11.1 26 2E No 12.8 121 2F Yes 12.8 20
    [0027]EXAMPLE 3
    [0028]Mesotrione was crystallised from samples taken from the plant during the solvent distillation. The effects of varying the starting pH of the crystallisation and purging the headspace of the crystallisation vessel with nitrogen were looked at. Samples were taken from the same batch after both 4500 lbs steam (distillation not finished) and 5045 lbs steam (distillation finished) has been used during the distillation. The pH of the sample was adjusted and the samples were crystallised via standard lab procedures. Total CN was measured by titration of the wet paste or filtrate. The results are shown in table 3.
    [0029]TABLE 3 Starting Total CN % reduction Distil- pH of content of in cyanide Example lation crystalli- N 2 wet paste content from No. Complete sation purge? (PPM) control 3A No 5.2 No 311 Control 3B Yes 5.2 No 236 Control 3C No 9.5 No 91 70 3D Yes 9.5 No 63 74 3E No 11.0 No 20 94 3F Yes 11.0 No 50 79 3G No 13 No 15 95 3H Yes 13 No 56 76 3I No 5.2 Yes 294 Control 3J No 11.0 Yes 46 85 3K No 11.3 Yes 15 95
    [0030]EXAMPLE 4
    [0031]This example looks at the cyanide content of mesotrione crystallised from different feed pH in a continuous crystallisation. The results are shown in Table 4.
    [0032]TABLE 4 pH of feed % Reduction in to Total CN Cyanide Content Sample crystalliser (ppm) from Control 7 th (final) sample from 5.0 217 Control crystalliser 7 th (final) sample from 5.0 181 Control crystalliser 7 th (final) sample from 11 15 92-93 crystalliser Final sample from crystalliser 11 15 92-93 Final sample from crystalliser 11 15 92-93 Final sample from crystalliser 9.5 15 92-93
    [0033]EXAMPLE 5
    [0034]Mesotrione was produced from the acid chloride by a standard condensation/rearrangement reaction. After the condensation/rearrangement reaction, water was added and the pH was adjusted to >11 and held for ½ hour. The pH was then adjusted to ˜5, the mixture distilled and then batch crystallised from either pH 5 or 9.5. The results are shown in Table 5.
    [0035]TABLE 5 pH held at after condensation/ Total CN in Example rearrangement Starting pH of mesotrione No. reaction crystallisation (ppm) 5A 11.9 5.0 15 5B 11.3 9.5 40
    [0036]EXAMPLE 6
    [0037]A large sample of mesotrione was obtained at the end of the distillation. This sample was divided into aliquots which were adjusted to a pH >11. A series of batch samples were made up and held agitated at the given pH for the amount of time specified in the table before being quickly adjusted to pH 2.4, filtered, washed and submitted for total cyanide analysis. The results are shown in Table 6.
    [0038]TABLE 6 Example Time kept at Total CN of No. Starting pH starting pH (min) mesotrione (ppm) 6A 11.6 0 111 6B 11.3 5 76 6C 11.5 10 72 6D 11.6 15 73 6E 11.5 20 55 6F 11.5 25 72 6G 11.4 30 76 6H 11.7 60 15 6I 12.3 90 15
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