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    • 2. 发明申请
    • METHOD OF RECOVERING ENERGY FROM WASTE LIQUORS FROM PULP PROCESSES
    • 从废纸处理中回收废物的能量的方法
    • WO1992018690A1
    • 1992-10-29
    • PCT/FI1992000092
    • 1992-03-31
    • A. AHLSTROM CORPORATIONNIKKANEN, Samuli
    • A. AHLSTROM CORPORATION
    • D21C11/12
    • D21C11/12D21C11/06Y02P70/24
    • Method of recovering energy from waste liquors from pulp processes, wherein the waste liquor is burned in a waste liquor recovery boiler and energy is recovered from the flue gases, which are formed by producing saturated or partially superheated steam in the recovery boiler. According to the invention, a portion of the waste liquor is pressure heat treated to release gases and/or treated in a liquid phase in a pressurized process for converting the waste liquor into a fraction containing an oleaginous fuel and a fraction containing inorganic components. The waste liquor is thereby treated for instance in a hydrogenation process. The waste liquor from the pressure heat treatment and/or the waste liquor fraction containing inorganic components is burned in the recovery boiler. The released gases and/or the fraction containing oleaginous fuel is burned in a separate superheating boiler, in which the steam produced in the recovery boiler is superheated.
    • 从废纸回收废液中回收来自纸浆工艺的废液的方法,其中废液在废液回收锅炉中燃烧并从废气中回收能量,废气通过在回收锅炉中产生饱和或部分过热蒸汽而形成。 根据本发明,一部分废液经加压热处理以在用于将废液转化为含有含油燃料的馏分和含有无机成分的馏分的加压方法中以液相释放和/或处理。 因此,例如在氢化过程中处理废液。 来自压力热处理的废液和/或含有无机成分的废液馏分在回收锅炉中燃烧。 释放的气体和/或含有油质燃料的馏分在单独的过热锅炉中燃烧,其中回收锅炉中产生的蒸汽过热。
    • 3. 发明申请
    • ELECTRONIC POWER CONTROL HAVING A SWITCHED-MODE POWER SUPPLY
    • 具有开关电源的电子电源控制
    • WO1998018199A1
    • 1998-04-30
    • PCT/FI1997000630
    • 1997-10-17
    • A. AHLSTROM CORPORATIONSAIRANEN, MarttiSALONEN, Olli
    • A. AHLSTROM CORPORATION
    • H02M07/538
    • H05B39/045H02M7/53803Y02B20/142
    • The present invention relates to an electronic power control with a switched-mode power supply, especially for a dimmer application. The power control comprises a half bridge control unit (2) having an oscillator circuit (5) and two control units (6, 7) and at least two switching elements, such as field effect transistors (8, 9) being preferably arranged in a half bridge configuration and which are connected by their gates to the outputs of the control units (6, 7) of the half bridge control unit (2). The switching time of the switching elements (8, 9), and thereby also the electrical power fed to the load (K), can be changed by changing the duty cycle of the oscillator circuit (5) output voltage. The half bridge control unit (2) is provided with terminals (5a, 5b) for connecting external components, especially a resistor and a capacitor thereto for setting the operating frequency of the half bridge control unit. According to the invention, the operating frequency terminals (5a, 5b) of the half bridge control unit (2) are provided with an active resistor circuit (14) and a capacitor (14), known as such. The active resistor circuit (14) comprises two adjustable resistors (16, 17), the first (16) of which is arranged to operate when the capacitor (15) is being charged and the second (17) of which is arranged to operate when the capacitor (15) is being discharged.
    • 本发明涉及具有开关式电源的电子功率控制,特别是用于调光器应用。 功率控制包括具有振荡器电路(5)和两个控制单元(6,7)的半桥控制单元(2),并且至少两个开关元件,例如场效应晶体管(8,9)优选地布置在 半桥配置,并通过其门连接到半桥控制单元(2)的控制单元(6,7)的输出端。 可以通过改变振荡电路(5)的输出电压的占空比来改变开关元件(8,9)的开关时间,从而也可以改变馈送到负载(K)的电力。 半桥式控制单元(2)设置有用于连接外部部件的端子(5a,5b),特别是用于设定半桥式控制单元的工作频率的电阻器和电容器。 根据本发明,半桥控制单元(2)的工作频率端子(5a,5b)设置有有源电阻电路(14)和电容器(14)。 有源电阻电路(14)包括两个可调电阻器(16,17),其中第一(16)被布置成在电容器(15)被充电时工作,并且其中第二(17)被布置成在 电容器15被放电。
    • 6. 发明申请
    • BLEACHING PULP WITH PEROXIDE AT SUPERATMOSPHERIC PRESSURE AND IN MULTIPLE STAGES
    • 在超级压力和多个阶段过氧化氢漂白浆
    • WO1996023929A1
    • 1996-08-08
    • PCT/FI1995000138
    • 1995-03-14
    • A. AHLSTROM CORPORATIONHENRICSON, KajGREENWOOD, BrianSVEDIN, BjörnPIKKA, Olavi
    • A. AHLSTROM CORPORATION
    • D21C09/16
    • D21C9/163
    • Cellulose pulp is bleached with peroxide under superatmospheric pressure in two (or more) stages, with removal of oxygen and reaction gases from the pulp between the stages, About 5-20 Kg/admt hydrogen peroxide is intimately mixed with the pulp and then introduced into a first pressurized vessel in which the pressure is between about 5-15 bar and the temperature between about 80-120 DEG C. Bleaching takes place in the first vessel for about 15-60 minutes while oxygen and reaction gases are formed, and then at least 20 % of (and preferably subtantially all of) the oxygen and reaction gases are removed from the pulp before complete consumption of all of the peroxide. Then the pulp is preferably introduced into a second vessel, additional peroxide, alkali, and steam can be added, and peroxide bleaching continues at a pressure of about 1.1-10 bar and at a temperature of about 90-120 DEG C for between about 30-200 minutes, during which oxygen and reaction gases are formed anew. The majority of the newly formed oxygen and reaction gases -- in fact subtantially all of them -- are separated out, typically upon discharge of the pulp from the second vessel.
    • 纤维素纸浆在两个(或多个)阶段的超大气压下用过氧化物漂白,除去来自阶段之间的纸浆的氧气和反应气体,约5-20Kg / adm过氧化氢与纸浆密切混合,然后引入 第一加压容器,其中压力在约5-15巴之间,温度在约80-120℃之间。漂白在第一容器中发生约15-60分钟,同时形成氧气和反应气体,然后在 在完全消耗所有过氧化物之前,至少20%(并且优选地是全部)氧和反应气体从纸浆中除去。 然后将纸浆优选引入第二容器中,可以加入额外的过氧化物,碱和蒸汽,并且过氧化物漂白在约1.1-10巴的压力和约90-120℃的温度下继续进行约30 -200分钟,在此期间重新形成氧气和反应气体。 大多数新形成的氧和反应气体 - 实际上基本上都是它们 - 被分离出来,通常在从第二容器排出纸浆时。
    • 9. 发明申请
    • A METHOD OF PURIFYING GASES CONTAINING NITROGEN OXIDES AND AN APPARATUS FOR PURIFYING GASES IN A STEAM GENERATION BOILER
    • 含有氮氧化物的气体的方法和用于在蒸汽发生炉中净化气体的装置
    • WO1995027554A1
    • 1995-10-19
    • PCT/FI1995000207
    • 1995-04-12
    • A. AHLSTROM CORPORATION
    • A. AHLSTROM CORPORATIONHILTUNEN, MattiLEE, YamVIEL LAMARE, Charles
    • B01D53/56
    • F23C10/10B01D53/56B01D53/8625F23J15/02F23J2215/10F23J2219/10F23J2219/20
    • A method of reducing the nitrogen oxide level in the flue gases issuing from combustion units by introduction of reducing agents into contact with gases containing nitrogen oxides in first and second reducing stages, is provided. The first reducing stage is a non-catalytic stage (e.g. at temperatures over 800 DEG C), while the second stage is a catalytic stage (e.g. at temperatures of about 300-400 DEG C). A steam generation boiler with improved nitrogen reduction facilities is also provided. The amount of nitrogen oxides in the hot gases is reduced in the combination of the first and second reducing stages while producing steam in a steam generation boiler system, thus resulting in gases essentially free from nitrogen oxides while eliminating the possibility of NH3 (or other reducing agent) slip in the exhausted flue gases. Heat transfers in a convection section are used to establish stabilized temperature conditions for catalytic reduction.
    • 提供了一种通过在第一和第二还原阶段通过引入还原剂与含有氮氧化物的气体接触来降低从燃烧单元排出的烟道气中的氮氧化物含量的方法。 第一还原阶段是非催化阶段(例如在800℃以上的温度),而第二阶段是催化阶段(例如在约300-400℃的温度)。 还提供了具有改进的氮还原设备的蒸汽发生锅炉。 在第一和第二还原阶段的组合中,在蒸汽发生锅炉系统中产生蒸汽的同时,热气中的氮氧化物的量减少,从而导致基本上不含氮氧化物的气体,同时消除了NH 3(或其它还原 试剂)在耗尽的烟道气中滑移。 使用对流段中的热传递建立稳定的催化还原温度条件。