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    • 1. 发明授权
    • Multistage spray drying method for detergent slurry
    • 洗涤剂浆液的多级喷雾干燥方法
    • US4261793A
    • 1981-04-14
    • US735501
    • 1976-10-26
    • Masayoshi NakamuraSeizi AbeTakeshi Arai
    • Masayoshi NakamuraSeizi AbeTakeshi Arai
    • B01J2/04B01D1/18C11D11/02F26B3/12B01D1/16
    • C11D11/02
    • A method is provided for spray drying a detergent slurry in a spray drying chamber having at least two different levels of uniformly spaced atomizing nozzles, which slurry consists of about 50 to 70% by weight of solid constituent comprising 20 to 40% by weight of active ingredient containing an anionic surfactant, 5 to 30% by weight of water-soluble silicate and at most 21% by weight of phosphate builder and about 50 to 30% by weight of water. The lower stage of the two adjoining spraying stages is positioned at a point in the spray drying chamber where the moisture content of the particles sprayed from the upper spraying stage becomes less than about 25% by weight. The lowest spraying stage is positioned at a point in the spray drying chamber which is at a temperature of from higher than the boiling point of the detergent slurry to less than 200.degree. C. From 30 to 70% of the slurry is sprayed from said lowest stage. There can be obtained a granular detergent which is an excellent granular material by this method.
    • 提供了一种用于在具有至少两个不同水平的均匀间隔的雾化喷嘴的喷雾干燥室中喷雾干燥洗涤剂浆料的方法,该浆料由约50至70重量%的固体成分组成,包含20至40重量%的活性 含有阴离子表面活性剂的成分,5至30重量%的水溶性硅酸盐和至多21重量%的磷酸盐助洗剂和约50至30重量%的水。 两个相邻的喷洒阶段的下阶段位于喷雾干燥室中从上喷涂阶段喷射的颗粒的水分含量小于约25重量%的点处。 最低喷涂阶段位于喷雾干燥室中的一个点处,该喷雾干燥室的温度高于洗涤剂浆液的沸点至小于200℃。从所述最低的喷雾干燥室喷射30-70%的浆料 阶段。 通过该方法可以得到粒状洗涤剂,其为优良的粒状物质。
    • 4. 发明申请
    • Charge pump
    • 电荷泵
    • US20110068856A1
    • 2011-03-24
    • US12807849
    • 2010-09-15
    • Masato MiyazakiHirotaka KawaiTatsuya KishiiMasayoshi NakamuraKen Makino
    • Masato MiyazakiHirotaka KawaiTatsuya KishiiMasayoshi NakamuraKen Makino
    • G05F3/02
    • H02M3/07
    • A charge pump includes a switching circuit which is interposed among first and second output capacitors, a flying capacitor, and an input power supply; and a control unit which controls the switching circuit. The charge pump is operated in an operation mode including a high-voltage outputting mode, a low-voltage outputting mode, and a relay mode. The control unit controls the switching circuit so that respective charging voltages of the first and second capacitors that are charged in the high-voltage outputting mode are gradually lowered. The control unit changes the operation mode of the charge pump by relay transition from the high-voltage outputting mode through the relay mode to the low-voltage outputting mode when a voltage lower command is given during a period when the operation mode of the charge pump is in the high-voltage outputting mode.
    • 电荷泵包括插入在第一和第二输出电容器之间的开关电路,飞跨电容器和输入电源; 以及控制开关电路的控制单元。 电荷泵在包括高压输出模式,低压输出模式和继电器模式的操作模式下操作。 控制单元控制开关电路,使得以高电压输出模式充电的第一和第二电容器的各自的充电电压逐渐降低。 当在电荷泵的操作模式期间给出电压较低的指令时,控制单元通过从高压输出模式通过继电器模式到低电压输出模式的继电器转换来改变电荷泵的操作模式 处于高电压输出模式。
    • 7. 发明授权
    • Method for granulating cationic surfactant
    • 阳离子表面活性剂造粒方法
    • US4510073A
    • 1985-04-09
    • US510243
    • 1983-07-01
    • Noboru HaraShinichi FukudomeNobuo JohnaMasayoshi Nakamura
    • Noboru HaraShinichi FukudomeNobuo JohnaMasayoshi Nakamura
    • B01F17/18C11D1/62C11D17/06A23L1/00
    • C11D17/06C11D1/62
    • A method for granulating a cationic surfactant having good water dispersibility and good storage stability comprising the steps of:(i) mixing 100 parts by weight of a powdered di (long-chain alkyl) quaternary ammonium salt having an average particle diameter of 150 .mu.m or less with 10 to 30 parts by weight of finely divided silica having an average primary particle diameter of 0.1 .mu.m or less;(ii) adding 20 to 80 parts by weight of a self-adhesive substance to the resultant mixture in the step (i), followed by granulation; and(iii) adding 30 to 150 parts by weight of at least one member selected from the group consisting of finely divided zeolite having an average primary particle diameter of 0.1 to 10 .mu.m, finely divided calcium carbonate having an average primary particle diameter of 0.01 to 10 .mu.m, and a mixture thereof, followed by granulation.
    • 将具有良好的水分散性和良好储存稳定性的阳离子表面活性剂造粒的方法包括以下步骤:(i)将100重量份平均粒径为150μm的二(长链烷基)季铵盐粉末 以下,10〜30重量份的平均一次粒径为0.1μm以下的细碎二氧化硅, (ii)在步骤(i)中向所得混合物中加入20至80重量份的自粘物质,然后造粒; 和(iii)添加30〜150重量份的选自平均一次粒径为0.1〜10μm的细分散沸石中的至少一种,平均一次粒径为0.01的细分碳酸钙 至10μm,其混合物,然后造粒。
    • 8. 发明授权
    • Process for producing granular detergent composition
    • 生产颗粒洗涤剂组合物的方法
    • US4478735A
    • 1984-10-23
    • US376963
    • 1982-05-11
    • Mitsuyoshi YazakiHideo TanakaMasayoshi Nakamura
    • Mitsuyoshi YazakiHideo TanakaMasayoshi Nakamura
    • C11D3/12C11D11/02C11D3/04B01D1/16
    • C11D11/02C11D3/128Y10S159/14
    • A process for producing a granular detergent composition containing a surface active agent, a zeolite, an alkali metal silicate, and other detergent builder is described. This granular detergent composition is produced by either (1)(a) preparing an aqueous slurry containing, as a dispersing medium, the surface active agent;(b) bubbling a gas into the aqueous slurry to form a slurry containing bubbles having an average bubble diameter of 40 through 100 microns and having a specific gravity of 0.7 through 0.9;(c) mixing the resultant aqueous slurry with the zeolite, the alkali metal silicate, and the other builders to form a detergent slurry; and(d) spray drying the detergent slurry to form the granular detergent composition or (2)(a) preparing a detergent slurry containing the surface active agent, the zeolite, the alkali metal silicate, and/or other detergent builders;(b) passing the detergent slurry through a centrifugal pump, while a gas is bubbled into the detergent slurry, whereby the detergent slurry containing bubbles having an average diameter of 40 through 100 microns and having a specific gravity of 0.7 through 0.9 is formed; and(c) spray drying the detergent slurry to form the granular detergent composition.
    • 描述了一种制备含有表面活性剂,沸石,碱金属硅酸盐和其它洗涤剂助洗剂的颗粒洗涤剂组合物的方法。 这种颗粒状洗涤剂组合物通过(1)(a)制备含有作为分散介质的表面活性剂的含水浆料来制备; (b)将气体鼓泡到含水浆料中以形成含有气泡直径为40-100微米,比重为0.7至0.9的气泡的浆料; (c)将所得含水浆料与沸石,碱金属硅酸盐和其它助洗剂混合以形成洗涤剂浆液; 和(d)喷雾干燥洗涤剂浆料以形成颗粒状洗涤剂组合物或(2)(a)制备含有表面活性剂,沸石,碱金属硅酸盐和/或其它洗涤剂助洗剂的洗涤剂浆料; (b)使清洁剂浆液通过离心泵,同时使气体鼓泡到洗涤剂浆液中,由此形成含有平均直径为40-100微米,比重为0.7至0.9的气泡的洗涤剂浆液; 和(c)喷雾干燥洗涤剂浆料以形成粒状洗涤剂组合物。
    • 10. 发明授权
    • Clock extracting device of a disc reproducing apparatus having a gain command unit for designating a loop gain
    • 具有用于指定环路增益的增益指令单元的盘再现装置的时钟提取装置
    • US07075866B2
    • 2006-07-11
    • US09986671
    • 2001-11-09
    • Masayoshi NakamuraEmi Kitano
    • Masayoshi NakamuraEmi Kitano
    • G11B5/09G11B7/005
    • G11B20/1025G11B5/012G11B7/0053G11B11/10515G11B20/1403H03L7/087H03L7/0898H03L7/093H03L7/113
    • A clock extracting device of a disc reproducing apparatus includes an information read-out member for reading information signals from a disklike information recording medium; a voltage control oscillator; a phase comparator; a frequency comparator; a speed sensor for detecting the frequency of the output of the voltage control oscillator at a reference clock so as to output a speed signal; a gain command unit for designating a loop gain of a clock extracting circuit in accordance with the speed signal outputted from the speed sensor; a charge pump which discharges or draws electric current in accordance with outputs of the phase comparator and the frequency comparator and changes over an output current value in accordance with a gain command of the gain command unit; and a series circuit of a resistor and a capacitor, wherein the gain command unit issues the gain command such that the loop gain of the clock extracting circuit secures a desired operating point in accordance with a read rate of the information signals.
    • 盘再现装置的时钟提取装置包括用于从盘状信息记录介质读取信息信号的信息读出部件; 压控振荡器; 相位比较器 频率比较器 速度传感器,用于在参考时钟处检测所述电压控制振荡器的输出频率,以便输出速度信号; 增益指令单元,用于根据从速度传感器输出的速度信号指定时钟提取电路的环路增益; 电荷泵,其根据相位比较器和频率比较器的输出放电或抽取电流,并根据增益指令单元的增益指令改变输出电流值; 以及电阻器和电容器的串联电路,其中所述增益命令单元发出所述增益命令,使得所述时钟提取电路的环路增益根据所述信息信号的读取速率来确保期望的工作点。