会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 2. 发明授权
    • Premixing swirling burner
    • 预旋转燃烧器
    • US4587809A
    • 1986-05-13
    • US677244
    • 1984-12-03
    • Takashi OhmoriIsao SatoYoji IshibashiYoshimitsu MinakawaMichio KurodaZensuke Tamura
    • Takashi OhmoriIsao SatoYoji IshibashiYoshimitsu MinakawaMichio KurodaZensuke Tamura
    • F23D14/02B01F5/04F23C6/04F23C15/00F23C99/00F23D14/62F23D14/82F23R3/34F02C1/00F02G3/00
    • F23C15/00B01F5/0451F23C6/042F23D14/62F23D14/82F23R3/346
    • A premixing swirling burner including a burner body having a swirling member at one end for causing fuel introduced into the burner body to flow in vortical form through the swirling member, a burner outer frame mounting the burner body and communicated with an air line for introducing air into the burner body, and a cylindrical member located in the burner outer frame for enclosing the burner body, with an air passage being defined between the inner periphery of the cylindrical member and an outer periphery of a portion of the burner body. A premixing chamber is defined between an outer periphery of a central portion of the burner body and an inner periphery of the cylindrical member for providing a fuel-air premix flowing toward the swirling member. A fuel chamber introduces fuel into the interior of the burner body, and a fuel ejection nozzle is located along an outer surface of the central portion of the burner body. A channel defined between the inner periphery of an end portion of the cylindrical member and an outer peripheral portion of the burner body formed an inlet for the premixing chamber has a cross-sectional area smaller than a cross-sectional area of the air passage.
    • 一种预混合旋转燃烧器,包括一端具有旋转构件的燃烧器主体,用于使引入燃烧器本体的燃料通过旋转构件以涡卷形式流动;燃烧器外框架,其安装燃烧器主体并与用于引入空气的空气管路连通 和位于燃烧器外框架中的圆筒形构件,用于封闭燃烧器主体,空气通道限定在圆柱形构件的内周和燃烧器本体的一部分外周之间。 在燃烧器主体的中心部分的外周和圆柱形部件的内周之间限定预混合室,用于提供朝向旋转部件流动的燃料 - 空气预混物。 燃料室将燃料引入燃烧器本体的内部,并且燃料喷射嘴位于燃烧器本体的中心部分的外表面。 形成在圆筒形构件的端部的内周和形成为预混合室的入口的燃烧器主体的外周部之间的通道的横截面积小于空气通道的横截面面积。
    • 3. 发明授权
    • Gas turbine combustor
    • 燃气轮机燃烧器
    • US4429538A
    • 1984-02-07
    • US234015
    • 1981-02-12
    • Isao SatoYohji IshibashiYoshimitsu MinakawaTakashi OhmoriZensuke TamuraYoshihiro UchiyamaRyoichiro Ohshima
    • Isao SatoYohji IshibashiYoshimitsu MinakawaTakashi OhmoriZensuke TamuraYoshihiro UchiyamaRyoichiro Ohshima
    • F23R3/04F23R3/06F23R3/12F23R3/14F23R3/34F02C3/14
    • F23R3/06F23R3/12
    • A gas turbine combustor comprising a combustor inner-pipe for forming a head combustion chamber and a rear combustion chamber having a diameter larger than a diameter of head combustion chamber. A combustor outer-pipe covers the combustor inner-pipe, and a fuel nozzle is disposed at an end part of the head combustion chamber for supplying fuel to said combustor inner pipe. A first group of ports are arranged for swirling and feeding air in an axial direction of the combustor inner-pipe. The first group of ports are around the fuel nozzle. A second group of ports for swirling and feeding air in a radial direction of said combustor inner-pipe are disposed in a side wall of the head combustion chamber near the fuel nozzle. A third group of ports for swirling and feeding air in a radial direction of the combustion inner-pipe and a fourth group of ports for feeding air in a radial direction of the combustor inner-pipe are provided and ar both disposed in a side wall of the head combustion chamber near the said rear combustion chamber. A fifth group of ports are disposed in a side wall of the rear combustion chamber near the head combustion chamber and a sixth group of ports are disposed in a side wall of the rear combustion chamber on a downstream side of the fifth group of ports. Another group of ports for swirling and feeding air into the head combustion chamber are disposed in a vicinity of a central portion of an end part of the head combustion chamber along an inner periphery of the fuel nozzle, with this group of ports and the first group of ports being constructed so that air flowing from both groups of ports has the same swirling direction.
    • 一种燃气轮机燃烧器,包括用于形成头部燃烧室的燃烧器内管和具有大于头部燃烧室直径的直径的后燃烧室。 燃烧器外管覆盖燃烧器内管,并且燃料喷嘴设置在头部燃烧室的端部,用于向燃烧器内管供应燃料。 第一组端口布置成在燃烧器内管的轴向上旋转和进给空气。 第一组港口在燃油喷嘴周围。 用于在所述燃烧器内管的径向方向上旋转和进给空气的第二组端口设置在靠近燃料喷嘴的头部燃烧室的侧壁中。 设置有用于在燃烧内管的径向上旋转和进给空气的第三组端口和用于沿着燃烧器内管的径向供给空气的第四组端口,并且ar设置在 靠近所述后燃烧室的头部燃烧室。 第五组端口设置在靠近头部燃烧室的后燃烧室的侧壁中,并且第六组端口设置在第五组端口的下游侧的后燃烧室的侧壁中。 用于将空气旋转并进入头部燃烧室的另一组端口沿着燃料喷嘴的内周设置在头部燃烧室的端部的中心部分的附近,该组端口和第一组 的端口被构造成使得从两组端口流出的空气具有相同的旋转方向。
    • 7. 发明授权
    • Method of fuel gasification and an apparatus for performing such a method
    • 燃料气化方法和执行这种方法的装置
    • US5676713A
    • 1997-10-14
    • US635285
    • 1996-04-19
    • Shozo NakamuraYasuaki AkatsuZensuke TamuraToru KobashiToshihiko Sasaki
    • Shozo NakamuraYasuaki AkatsuZensuke TamuraToru KobashiToshihiko Sasaki
    • C10J3/46C10J3/48C10J3/52C10J3/86C10J3/84
    • C10J3/485C10J3/86C10J2300/093C10J2300/1884Y02P20/124Y10S48/02
    • In fuel gasification, particles of, for example, coal and an oxidant are supplied to a reactor, where the coal particles are gasified. The gas thus produced may contain molten slag entrained therein and such slag could subsequently solidify and affect other components of the coal gasification apparatus. Therefore a molten slag cooling heat exchanger is positioned directly above the reactor and this cools the gas so as to cause any molten slag therein to solidify. Hence, such molten slag does not reach an evaporator above the molten slag cooling heat exchanger, so that the efficiency of the evaporator will be maintained. However, solidified molten slag may build up on heat exchange tubes of the molten slag cooling heat exchanger. Therefore, the rate of coolant supplied to the molten slag cooling heat exchanger is varied, to cause expansion and contraction which causes solidified slag to be dislodged. Hence the efficiency of the molten slag cooling heat exchanger does not deteriorate. Cleaning gas and coal particles may be jetted onto the evaporator to dislodge ash or soot therefrom.
    • 在燃料气化中,将例如煤和氧化剂的颗粒供给到煤颗粒气化的反应器中。 由此产生的气体可能含有夹带在其中的熔渣,并且这种炉渣随后可能固化并影响煤气化装置的其它组分。 因此,熔渣冷却热交换器直接位于反应器上方,并且冷却气体,以使其中的任何熔融炉渣固化。 因此,这种熔渣不会在熔渣冷却热交换器上方到达蒸发器,从而保持蒸发器的效率。 然而,固化的熔融炉渣可能积聚在熔渣冷却热交换器的换热管上。 因此,提供给熔渣冷却热交换器的冷却剂的比例变化,引起膨胀和收缩,这导致固化的炉渣脱落。 因此,熔渣冷却用热交换器的效率不会降低。 可以将清洁气体和煤颗粒喷射到蒸发器上以从其中排出灰分或烟灰。
    • 8. 发明授权
    • Process and apparatus for purifying raw coal gas
    • 原煤气净化工艺及装置
    • US4233275A
    • 1980-11-11
    • US965512
    • 1978-12-01
    • Shoichi KimuraToshihiko TakahashiZensuke Tamura
    • Shoichi KimuraToshihiko TakahashiZensuke Tamura
    • C10K1/04C10K1/20C10K1/34B01D53/34
    • C10K1/34C10K1/04C10K1/20
    • A high temperature, high pressure raw coal gas containing hydrogen sulfide, ammonia, and tarry matter, is purified by contacting the raw coal gas with solid particles thereby cooling the raw coal gas to a temperature suitable for hydrogen sulfide removal and at the same time depositing the tarry matter onto the solid particles by condensation to recover the tarry matter from the raw coal gas, removing the hydrogen sulfide from the cooled and substantially tar-free coal gas, expanding the raw coal gas to a pressure suitable for ammonia decomposition, heating the expanded raw coal gas to a temperature suitable for ammonia decomposition by heat obtained by combusting the recovered tarry matter on the solid particles, thereby regenerating the solid particles for reuse, and then decomposing ammonia in the raw coal gas, thereby removing ammonia therefrom. A process for efficiently purifying raw coal gas by removing tarry matter, hydrogen sulfide and ammonia, including effectively utilizing the recovered tarry matter to produce heat while also effectively utilizing the energy obtained by expanding the coal gas through a pressure-reducing means such as an expansion turbine.
    • 通过使原煤气与固体颗粒接触,将硫化氢,氨和焦油状物的高温,高压原煤气体纯化,从而将原煤气体冷却至适于除去硫化氢的温度,同时沉积 通过冷凝将固体颗粒的焦油状物从原煤气中回收焦油物质,从冷却和基本上无焦油的煤气中除去硫化氢,将原料气扩展至适于氨分解的压力,加热 通过将固体颗粒上回收的焦油物质燃烧而获得的热量将原煤气体膨胀至适于氨分解的温度,从而再生固体颗粒再利用,然后分解原煤气中的氨,从而从其中除去氨。 一种通过去除焦油物质,硫化氢和氨来有效净化原煤的方法,包括有效地利用回收的焦油物质产生热量,同时还有效地利用通过诸如膨胀的减压装置膨胀煤气而获得的能量 涡轮。
    • 9. 发明授权
    • Apparatus for elimination of nitrogen oxides from combustion waste gases
    • 用于从燃烧废气中去除氮氧化物的装置
    • US4003711A
    • 1977-01-18
    • US514130
    • 1974-10-11
    • Yukio HishinumaHidetoshi AkimotoZensuke TamuraFumito Nakajima
    • Yukio HishinumaHidetoshi AkimotoZensuke TamuraFumito Nakajima
    • B01D53/86B01D53/94B01J8/18B01J27/00B01J27/043B01J27/28B01J38/48F23J15/00B01J8/12B01J23/94F01N3/15
    • B01J23/94B01D53/9413B01J38/485F23J15/00B01D2251/2062B01D2255/20707B01D2255/20738
    • Nitrogen oxides (NOx) are removed from combustion waste gases by injecting gas (NH.sub.3) into the combustion waste gases in the presence of a metallic catalyst to deoxidize the nitrogen oxides to nitrogen and water, within a reaction tower having the catalysts moving through the reaction tower, so that thereafter the dust may be separated from the catalysts and the catalysts may be regenerated continuously, so that the regenerated catalysts may be returned to the reaction tower. The catalyst moves in a substantially closed path, and preferable downwardly through the reaction tower, with the ammonia gas and combustion waste gases moving in cross current through the reaction tower, with mixing being enhanced by a plurality of angled baffle plates. Regeneration is accomplished by washing the catalysts, particularly ferrous catalysts with water to remove ferric sulfates, thereafter providing ferrous sulfates on the surface of the ferrous catalysts, and thereafter heating the catalysts with combustion gases separate from the ammonia gases, to dry the catalysts prior to their moving into the portion of the reaction tower having therein the mixed ammonia gas and combustion waste gases.
    • 通过在催化剂移动通过反应的反应塔内,在金属催化剂的存在下将气体(NH 3)注入到燃烧废气中以将氮氧化物氧化成氮和水,从而从燃烧废气中除去氮氧化物(NOx) 塔,从而可以将灰尘与催化剂分离,并且可以连续再生催化剂,使得再生催化剂可以返回到反应塔。 催化剂在基本上封闭的路径中移动,并且优选向下通过反应塔,氨气和燃烧废气在交叉电流中移动通过反应塔,混合通过多个成角度的挡板增强。 通过用水洗涤催化剂,特别是含铁催化剂以除去硫酸亚铁,然后在亚铁催化剂的表面上提供硫酸亚铁,然后用与氨气分离的燃烧气体加热催化剂,将催化剂干燥,然后在 它们进入其中具有混合氨气的反应塔部分和燃烧废气。
    • 10. 发明授权
    • Adsorption method
    • 吸附法
    • US3980454A
    • 1976-09-14
    • US545089
    • 1975-01-29
    • Yukio HishinumaZensuke TamuraSyunzi Enomoto
    • Yukio HishinumaZensuke TamuraSyunzi Enomoto
    • B01D53/04C01B17/775
    • B01D53/04C01B17/775B01D2253/102B01D2257/302B01D2259/40092
    • A contaminant, such as sulfur dioxide, is removed from a fluid, such as hot exhaust gas, by passing it through beds of material for removing the contaminants, such as activated carbon for adsorbing the sulfur dioxide as sulfur trioxide; periodically, the bed is regenerated by discontinuing the passage of process fluid therethrough and passing through the bed a regenerating fluid, such as water, with quantities of the regenerating fluid being successively passed through the bed with corresponding decreasing amounts of contaminants, such as sulfuric acid within the water, in the respective quantities of regenerative fluid. At least one further bed of material is regenerated with substantially the same regenerative fluid in substantially the same succession of concentrations, but out of phase so that a quantity of regenerative fluid of one contaminant concentration is passed completely through only one bed of material prior to its passing through another bed of material. Preferably, after passing through one bed of material, the regenerative fluid is of the next highest concentration and passes through another bed of material in the sequence of the next highest concentration.
    • 通过使其通过用于除去污染物的材料床(例如用于以二氧化硫吸附二氧化硫的活性炭)将诸如二氧化硫的污染物从诸如热废气的流体中除去; 周期性地,通过停止工艺流体的通过并通过床将再生流体例如水再生,使再生流体的量连续地通过床,同时减少量的污染物例如硫酸 在水中,各自的再生流体的量。 基本上相同的再生流体基本上以相同的一系列浓度再生至少一个另外的材料床,但是异相再生,使得一个污染物浓度的再生流体的量在其之前仅通过一个材料床 穿过另一张床。 优选地,在通过一个材料床之后,再生流体具有下一个最高浓度,并且以下一个最高浓度的顺序通过另一个材料床。