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    • 2. 发明专利
    • Treatment of coal ash
    • 煤炭治理
    • JPS5753225A
    • 1982-03-30
    • JP12880480
    • 1980-09-17
    • Electric Power Dev Co LtdKawasaki Heavy Ind Ltd
    • SHIRAKATA TADASHIMOURI KUNIHIKOITOU HAYAMIZUNAGAI CHIAKI
    • F23J15/00B01D53/94B09B3/00F23J1/00
    • PURPOSE: To effectively utilize coal ash by classifying said coal ash collected from an exhaust gas of a coal boiler in a dust collecting apparatus into a fine powder containing an ammonium compound and a crude powder containing black coal ash.
      CONSTITUTION: An exhaust gas of a coal boiler 1 is successively passed through a denitration apparatus 2, an air preheater 3, a dust collecting apparatus 4, a heat exchanger 5 and a desulfurization apparatus 6 to be treated. coal ash from which dust is removed in the dust collecting apparatus 4 is thrown into a classifier 11 to be classified into a fine powder containing an ammonium compound and a crude powder containing black ash. The ammonium compound is decomposed at 300W 500°C in an ammonium compound pyrolysis furnace 12 and the decomposed gas containing ammonia is separated in a solid-gas separator 14 to be reutilized in the ditration apparatus 2 as well as the separated coal ash is utilized in fly ash or the like. The crude powder is baked and decolorized at 500W1,100°C in a decoloring furnace 16 and transported to an ash treating installation through an ash coloer 17 to be effectively utilized.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:通过将从灰尘收集装置中的煤锅炉废气中收集的煤灰分为含有铵化合物的细粉和含有黑煤灰的粗粉,有效地利用煤灰。 构成:煤锅炉1的废气依次通过待处理的脱硝装置2,空气预热器3,集尘装置4,热交换器5和脱硫装置6。 将在灰尘收集装置4中除去灰尘的煤灰投入分级器11中,分类为含有铵化合物的细粉末和含有黑灰的粗粉末。 铵化合物在铵化合物热解炉12中在300-500℃下分解,含有氨的分解气体在固气分离器14中分离,以在脱水装置2中再利用,分离的煤灰为 用于飞灰等。 粗粉末在脱色炉16中在500-1100℃下被烘烤和脱色,并通过灰分颜料17输送到灰处理装置,以有效地利用。
    • 3. 发明专利
    • Treatment of coal ash
    • 煤炭治理
    • JPS5753224A
    • 1982-03-30
    • JP12880380
    • 1980-09-17
    • Electric Power Dev Co LtdKawasaki Heavy Ind Ltd
    • SHIRAKATA TADASHIMOURI KUNIHIKOITOU HAYAMIZUNAGAI CHIAKI
    • F23J15/00B01D53/94B09B3/00F23J1/00
    • PURPOSE: To efficiently remove an ammonium compound and black coal ash in coal ash respectively to utilize the same effectively by heating coal ash collected from an exhaust gas of a coal boiler in a dust collecting apparatus to a specific temp.
      CONSTITUTION: An exhaust gas from a coal boiler 1 is successively passed through a denitration apparatus 2, an air preheater 3, a dust collecting apparatus 4, a heat exchanger 5 and a desulfurization apparatus 6 to be treated. Coal ash from which dust is removed in the dust collecting apparatus 4 contains black coal ash and an ammonium compound. Said coal ash is thrown into an ammonium compound pyrolysis furnace 11 and subjected to solid-gas contact at 300W500°C to decompose said ammonium compound and a decomposed gas containing ammonia is separated in a solid-gas separator 13 to be utilized in the denitration apparatus 2. Further, separated coal ash is thrown into a classifier 14 to be classified into a fine powder and a crude powder containing black coal ash such as uncombusted carbon or the like. The crude powder is thrown into a decoloring furnace 15 to be baked at 500W 1,100°C and, after decoloring, transported to an ash treating installation through an ash cooler 16.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:为了有效地除去煤灰中的铵化合物和黑煤灰,通过将从灰尘收集装置中的煤锅炉的废气中收集的煤灰加热到特定温度来有效地利用煤灰灰分。 构成:来自煤锅炉1的排气依次通过待处理的脱硝装置2,空气预热器3,集尘装置4,热交换器5和脱硫装置6。 在灰尘收集装置4中除尘的煤灰含有黑煤灰和铵化合物。 将所述煤灰投入铵化合物热解炉11中,在300-500℃下进行固气接触,分解所述铵化合物,并在固气分离器13中分离含有氨的分解气体,以用于 脱硝装置2.此外,将分离的煤灰投入分级器14中以分级为细粉末和含有黑煤灰的粗粉末,例如未燃碳等。 将粗粉末投入脱色炉15中,在500-1100℃下烘烤,脱色后通过灰分冷却器16输送至灰处理装置。
    • 4. 发明专利
    • Rotary type heat exchanger
    • 旋转式热交换器
    • JPS5743195A
    • 1982-03-11
    • JP11837780
    • 1980-08-29
    • Electric Power Dev Co LtdGadelius Kk
    • YOSHIKAWA BUNKIYUUIKEDA NOBUICHISHIMIZU TATSUJIROUFURUKAWA MICHIYOSHIMOURI KUNIHIKO
    • B01D53/94F23J15/00F28D19/04
    • PURPOSE: To prevent a clogging phenomenon caused by an adhesion of acid ammonium sulfate by a method wherein a medical temperature part and a low temperature part in a rotary type heat exchanger are made to form an integral structure of a group of long thermo conductive elements having no interrupted part.
      CONSTITUTION: The thermo conductive elements of a rotary type heat exchanger are divided into a section 10 composed of short thermo conductive elements corresponding to the high temperature part and a section 14 of integral structure composed of long thermo conductive elements corresponding to the medial temperature and low temperature part so as to eliminate any interrupted part between the medial temperature section and the low temperature section. In this arrangement, a clogging phenomenon caused by an adhesion of acid ammonium sulfate generated at the interrupted part is prevented.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:为了防止酸性硫酸铵粘附引起的堵塞现象,其中将旋转型热交换器中的医用温度部分和低温部分制成一组长的热传导元件的整体结构, 没有中断的部分。 构成:旋转式热交换器的导热元件被分成由对应于高温部分的短导热元件组成的部分10和由对应于中间温度和低温的长导热元件组成的整体结构部分14 温度部分,以消除中间温度部分和低温部分之间的任何中断部分。 在这种布置中,防止了由在中断部分产生的酸式硫酸铵的粘附引起的堵塞现象。
    • 6. 发明专利
    • REMOVAL OF AMMONIUM COMPOUND FROM COAL ASH
    • JPS56161823A
    • 1981-12-12
    • JP6313580
    • 1980-05-13
    • KAWASAKI HEAVY IND LTDDENGEN KAIHATSU KK
    • ITOU HAYAMIZUNAGAI CHIAKIMOURI KUNIHIKOSHIRAKATA TADASHI
    • B01D53/94B09B3/00C01C1/02F23J15/00
    • PURPOSE:To contrive to save energy as well as to carry out stable coal burning waste gas treatment by a method wherein an NH3 compound in a coal ash is thermally decomposed by a high temp. combustion gas in the system and a decomposed gas is reutilized as an NH3 source of a denitrification apparatus. CONSTITUTION:A waste gas of a coal burning boiler 1 is treated by a system consisted of a denitrification apparatus 2, an air preheating apparatus 3, a low temp. dust collecting apparatus 4 and a desulfurization apparatus 6. In this case, a coal ash containing the NH3 compound discharged from the dust collecting apparatus is thrown into a thermal decomposition furnace 13 through an ash hopper 12 and said NH3 compound is thermally decomposed at a temp. of 250-700 deg.C by a high temp. combustion gas of the boiler 1. Then, the coal ash after the thermal decomposition and the decomposed gas are separated in a solid-gas separator 15 and the decomposed gas is returned to a position in front of the denitrification apparatus 2 to be reutilized as an NH3 source. On the other hand, the coal ash is cooled by air in a cooler 18 and, thereafter, transported to an ash treating installation 21. Further, air heated to about 200-500 deg.C after heat exchanged with the high temp. coal ash in the cooler 18 is blown into a coal ash transport pipe 11 of an upstream side of the furnace 13 and used as a source for transporting the NH3 containing coal ash.
    • 8. 发明专利
    • REMOVAL OF AMMONIUM COMPOUND FROM COAL ASH
    • JPS56161822A
    • 1981-12-12
    • JP6313480
    • 1980-05-13
    • KAWASAKI HEAVY IND LTDDENGEN KAIHATSU KK
    • ITOU HAYAMIZUNAGAI CHIAKIMOURI KUNIHIKOSHIRAKATA TADASHI
    • B01D53/94B09B3/00C01C1/02F23J15/00
    • PURPOSE:To unnecessitate a large thermal decomposition furnace of an NH3 compound and to thermally decompose the NH3 compound efficiently by thermally decomposing the NH3 compound in a coal ash while said coal ash is transported through an ash treating pipe. CONSTITUTION:A waste gas of a coal burning boiler 1 is treated by a system consisted of a denitrification apparatus 2, an air preheater 3, a low temp. dust collector 4 and a desulfurization apparatus 6. In this case, the coal ash collected in the dust collector 4 containing the NH3 compound (e.g. ammonium sulfate) discharged from the dust collector 4 is thrown into the ash treating pipe 12 as well as a high temp. combustion waste gas of the boiler 1 is introduced into the pipe 12 and said ash and gas are subjected to solid-gas contact to thermally decompose the NH3 compound in the coal ash. In this case, the temp. in said pipe is 250-700 deg.C. Subsequently, the coal ash after thermal decomposition and the decomposed gas are separated in a solid-gas separator 13 and the decomposed gas is returned to a position in front of the denitrification apparatus 2 to be reutilized as a NH3 source. On the other hand, the coal ash is cooled in a cooler and, thereafter, transported to an ash treating installation 20.