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    • 1. 发明授权
    • Method and apparatus for reclaiming oil from waste plastic
    • 从废塑料回收油的方法和设备
    • US6011187A
    • 2000-01-04
    • US945458
    • 1997-10-27
    • Hirotoshi HorizoeTakeshi AmariHiroshi NagaiShizuo YasudaYuji KaiharaYoshimasa KawamiYasumasa Matsukawa
    • Hirotoshi HorizoeTakeshi AmariHiroshi NagaiShizuo YasudaYuji KaiharaYoshimasa KawamiYasumasa Matsukawa
    • B29B17/02C10G1/00C10G1/02C10G1/10C10B1/04C08J1/16
    • B29B17/02C10G1/00C10G1/006C10G1/02C10G1/10B29B17/04B29B2017/0496B29K2027/06B29K2101/10Y02P70/26Y02W30/622Y02W30/625
    • This invention provides a method for reclaiming oil from waste plastic in such a way that thermosetting resins and solid foreign matter in the plastic will not pose a problem. This method greatly reduces the burden of presorting the garbage or industrial waste. To achieve this objective when oil is to be reclaimed from a waste plastic containing chlorine compounds, such as vinyl chloride, the plastic must first be stripped of chlorine. Prior to pyrolysis, while being conveyed forward in a continuous stream, the plastic is mixed with heated sand and/or an additive agent to raise its temperature to 250-350.degree. C. This creates a product which is comprised of a mixture of sand and substantially dechlorinated plastic. The product is mixed with heated sand to heat it directly to a temperature of 350-500.degree. C. It is maintained at this temperature until pyrolysis occurs. In order to obtain high-quality oil with a low boiling point, a first gas/liquid separation process separates the product obtained from the aforesaid pyrolysis into liquid high-boiling point oil, gaseous low-boiling point oil and low molecular-weight gases, and recirculates the liquid high-boiling point oil to the pyrolysis process, and a second gas/liquid separation process separates the gaseous low-boiling point oil and low molecular-weight gases into liquid low-boiling point oil and low molecular-weight gases. The first and second gas/liquid separation process are connected in sequence.
    • PCT No.PCT / JP97 / 00572 Sec。 371日期1998年1月8日 102(e)日期1998年1月8日PCT提交1997年2月27日PCT公布。 公开号WO97 / 31990 日期1997年9月4日本发明提供了一种从废塑料中回收油的方法,使得塑料中的热固性树脂和固体异物不会造成问题。 这种方法大大减轻了预处理垃圾或工业废物的负担。 为了达到这个目的,当油从含氯化合物(如氯乙烯)的废塑料中回收时,塑料必须先被除去氯。 在热解之前,当在连续流中向前输送时,将塑料与加热的砂和/或添加剂混合以将其温度升高至250-350℃。这产生了由砂和 基本上脱氯塑料。 将产物与加热的沙子混合,直接加热到350-500℃的温度。保持在该温度直到发生热解。 为了获得低沸点的优质油,第一气/液分离方法将从上述热分解得到的产物分离成液体高沸点油,气态低沸点油和低分子量气体, 并将液体高沸点油再循环到热解过程中,并且第二气/液分离过程将气态低沸点油和低分子量气体分离成液体低沸点油和低分子量气体。 第一和第二气/液分离过程依次连接。
    • 2. 发明申请
    • BIOCOKES PRODUCING METHOD AND APPARATUS
    • 生物制造方法和装置
    • US20120168296A1
    • 2012-07-05
    • US13250444
    • 2011-09-30
    • Tamio IDAYoshimasa KAWAMIJun SATOU
    • Tamio IDAYoshimasa KAWAMIJun SATOU
    • C10B47/00
    • C10B47/12C10B53/02C10L5/447C10L9/08Y02E50/10Y02E50/14Y02E50/30Y02P20/145
    • A method of producing biocokes in which pulverized biomass is fed and pressed in a reaction container is provided, wherein the pulverized biomass in a substantially-packed state is pressure-formed while being heated in a temperature range and a pressure range to obtain a semi-carbonized solid matter or pre-semi-carbonized solid matter and then cooled to produce biocoke. The method may includes a filling step; a reaction step; heating the pulverized biomass by means of a heating device to the temperature range and keeping such state for a prescribed period of time to form a shaped matter of the pulverized biomass in the reaction container, and then cooling the shaped matter by switching from the heating device to a cooling device; and an ejecting step.
    • 提供一种生产生物炭的方法,其中将粉碎的生物质在反应容器中进料和加压,其中将基本上填充状态的粉碎的生物质在加热温度范围和压力范围内进行压力成形, 碳化固体物质或预半碳化固体物质,然后冷却生产生物炭。 该方法可以包括填充步骤; 反应步骤 通过加热装置将粉碎的生物质加热到温度范围并保持这种状态一段规定的时间以在反应容器中形成粉碎生物质的成形物质,然后通过从加热装置切换冷却成形物质 到冷却装置; 和弹出步骤。
    • 3. 发明申请
    • BIOCOKE PRODUCING APPARATUS, METHOD OF CONTROLLING THE SAME AND PROCESS FOR PRODUCTION THEREOF
    • 生物制造装置,其控制方法及其生产方法
    • US20100205860A1
    • 2010-08-19
    • US12597618
    • 2008-04-18
    • Yoshimasa KawamiJun SatouTamio Ida
    • Yoshimasa KawamiJun SatouTamio Ida
    • C10L5/06B01J19/00
    • C10L5/44B30B11/005B30B11/26B30B15/34C10B47/32C10B53/02Y02E50/10Y02E50/14Y02E50/30Y02P20/145
    • A biocoke producing apparatus that realizes efficient mass production of biocoke; a method of controlling the same; and a process for manufacture thereof. The apparatus includes a horizontal tubular reaction vessel (10) provided on its one end side with a supply part (11) for pulverized biomass and provided on its other end side with a discharge part (12). On the supply part side, there is provided an extrusion piston (6) capable of reciprocation along the longitudinal direction in the interior of the reaction vessel and capable of pressurizing the pulverized biomass within the vessel; The temperature range and pressure range for inducing a pyrolytic or thermal curing reaction of lignin and hemicellulose contained in the pulverized biomass are preset, and the reaction vessel (10) is provided with a thermal reaction region (13) for heating the pulverized biomass at temperature within the above temperature range and with a cooling region (14). By means of the extrusion piston (6), not only is the pulverized biomass transferred so as to stay for a given period of time in each of the regions but also the pulverized biomass within the vessel is pressurized so as to fall within the above pressure range.
    • 实现生物炭的高效批量生产的生物炭生产设备; 一种控制它的方法; 及其制造方法。 该装置包括在其一端侧设置有用于粉碎生物质的供应部分(11)的水平管式反应容器(10),并在其另一端侧设置有排出部分(12)。 在供给部侧,设置有能够在反应容器的内部沿着长度方向往复运动并能够对容器内的粉碎生物质进行加压的挤出活塞(6) 预设用于诱导粉碎的生物质中包含的木质素和半纤维素的热解或热固化反应的温度范围和压力范围,并且反应容器(10)设置有用于在温度下加热粉碎的生物质的热反应区域(13) 在上述温度范围内并具有冷却区域(14)。 通过挤压活塞(6),不仅粉碎的生物质被转移以在每个区域中停留给定的时间段,而且容器内的粉碎的生物质也被加压以达到上述压力 范围。
    • 4. 发明申请
    • APPARATUS AND PROCESS FOR PRODUCING BIOCOKE
    • 生物识别的装置和方法
    • US20100133086A1
    • 2010-06-03
    • US12597603
    • 2008-04-22
    • Yoshimasa KawamiJun SatouAyumu YamazakiTamio Ida
    • Yoshimasa KawamiJun SatouAyumu YamazakiTamio Ida
    • C10B51/00
    • C10L5/44C10B47/12C10B47/28C10B53/02Y02E50/10Y02E50/14Y02E50/30Y02P20/145
    • An apparatus and process for producing biocoke usable as a substitute fuel for coal coke from biomass as a raw material. The apparatus comprises pulverizing means for pulverizing a biomass raw material attributed to photosynthesis; heating means for heating to the temperature range in which the hemicellulose of the pulverized biomass raw material is pyrolyzed so as to exhibit bonding effects; pressurization means for, in the state of the heating, pressurizing to the pressure range in which the lignin of the pulverized biomass exhibits a thermal curing reaction and maintaining the pressure; and cooling means for cooling after maintaining the state of the pressurization. The apparatus further comprises temperature detecting means provided at the exit end of the region being heated by the heating means and regulation means for judging a reaction terminal point in accordance with the result of the temperature detection and regulating the timing for transfer from heating to cooling.
    • 一种用于生产生物炭的设备和方法,其可用作煤焦油的替代燃料,其以生物质为原料。 该装置包括用于粉碎归因于光合作用的生物质原料的粉碎装置; 加热装置,其加热到粉碎的生物质原料的半纤维素被热解以显示粘合效果的温度范围; 加压装置,用于在加热状态下加压到粉碎生物质的木质素表现出热固化反应并保持压力的压力范围; 以及用于在保持加压状态之后冷却的冷却装置。 该装置还包括设置在由加热装置加热的区域的出口端处的温度检测装置和根据温度检测结果判断反应终点并调节从加热转移到冷却的时间的调节装置。
    • 5. 发明授权
    • Biocoke producing apparatus and process therefor
    • 生物炭生产设备及其工艺
    • US08460515B2
    • 2013-06-11
    • US12597662
    • 2008-04-22
    • Yoshimasa KawamiJun SatouTamio Ida
    • Yoshimasa KawamiJun SatouTamio Ida
    • C10B45/02C10L5/06C10L5/02
    • C10L5/02C10B47/12C10B53/02C10L5/447C10L9/083Y02E50/10Y02E50/14Y02E50/15Y02E50/30Y02P20/145
    • A biocoke producing apparatus has a reaction vessel that has a preset temperature range and pressure range for, without carbonizing of the pulverized biomass, inducing a pyrolytic or thermal curing reaction of lignin and hemicellulose thereof. The reaction vessel has a pressurization device for pressurizing to the pressure range, a heating device for heating to the temperature range in the state of the pressurization and a cooling device for cooling after maintaining of the above state. Multiple reaction vessels are provided. A pulverization delivery conveyor is provided superior to these reaction vessels, and each of the multiple reaction vessels is connected via a connection tube to the conveyor. The connection tube is provided with a pulverizate charging device for charging a given amount of pulverized biomass in accordance with a timing of pulverizate charging to the reaction vessels.
    • 生物炭制造装置具有反应容器,该反应容器具有预定的温度范围和压力范围,用于没有粉碎生物质的碳化,引起木质素和其半纤维素的热解或热固化反应。 反应容器具有对压力范围进行加压的加压装置,在加压状态下加热至温度范围的加热装置以及维持上述状态后的冷却装置。 提供多个反应容器。 提供优于这些反应容器的粉碎输送输送机,并且多个反应容器中的每一个通过连接管连接到输送机。 连接管设置有粉碎装料装置,用于根据向反应容器进行粉碎装料的时间对给定量的粉碎生物量进行加料。
    • 6. 发明授权
    • Method and apparatus for reclaiming oil from waste plastic
    • 从废塑料回收油的方法和设备
    • US06172271B2
    • 2001-01-09
    • US09438307
    • 1999-11-12
    • Hirotoshi HorizoeTakeshi AmariHiroshi NagaiShizuo YasudaYuji KaiharaYoshimasa KawamiYasumasa Matsukawa
    • Hirotoshi HorizoeTakeshi AmariHiroshi NagaiShizuo YasudaYuji KaiharaYoshimasa KawamiYasumasa Matsukawa
    • C10G100
    • B29B17/02B29B17/04B29B2017/0496B29K2027/06B29K2101/10C10G1/00C10G1/006C10G1/02C10G1/10Y02P70/26Y02W30/622Y02W30/625
    • This invention provides a method for reclaiming oil from waste plastic in such a way that thermosetting resins and solid foreign matter in the plastic will not pose a problem. This method greatly reduces the burden of presorting the garbage or industrial waste. To achieve this objective when oil is to be reclaimed from a waste plastic containing chlorine compounds, such as vinyl chloride, the plastic must first be stripped of chlorine. Prior to pyrolysis, while being conveyed forward in a continuous stream, the plastic is mixed with heated sand and/or an additive agent to raise its temperature to 250-350° C. This creates a product which is comprised of a mixture of sand and substantially dechlorinated plastic. The product is mixed with heated sand to heat it directly to a temperature of 350-500° C. It is maintained at this temperature until pyrolysis occurs. In order to obtain high-quality oil with a low boiling point, a first gas/liquid separation process separates the product obtained from the aforesaid pyrolysis into liquid high-boiling point oil, gaseous low-boiling point oil and low molecular-weight gases, and recirculates the liquid high-boiling point oil to the pyrolysis process, and a second gas/liquid separation process separates the gaseous low-boiling point oil and low molecular-weight gases into liquid low-boiling point oil and low molecular-weight gases. The first and second gas/liquid separation process are connected in sequence.
    • 本发明提供了一种从废塑料中回收油的方法,使得塑料中的热固性树脂和固体异物不会造成问题。 这种方法大大减轻了预处理垃圾或工业废物的负担。 为了达到这个目的,当油从含氯化合物(如氯乙烯)的废塑料中回收时,塑料必须先被除去氯。 在热解之前,当在连续流中向前输送时,将塑料与加热的砂和/或添加剂混合以将其温度升高至250-350℃。这产生了由砂和 基本上脱氯塑料。 将产物与加热的沙子混合,将其直接加热至350-500℃的温度。保持在该温度直至发生热解。 为了获得低沸点的优质油,第一气/液分离方法将从上述热分解得到的产物分离成液体高沸点油,气态低沸点油和低分子量气体, 并将液体高沸点油再循环到热解过程中,第二气/液分离过程将气态低沸点油和低分子量气体分离成液体低沸点油和低分子量气体。 第一和第二气/液分离过程依次连接。
    • 8. 发明申请
    • BIOCOKE PRODUCING APPARATUS AND PROCESS THEREFOR
    • 生物处理生产设备及其过程
    • US20100162618A1
    • 2010-07-01
    • US12597662
    • 2008-04-22
    • Yoshimasa KawamiJun SatouTamio Ida
    • Yoshimasa KawamiJun SatouTamio Ida
    • C10L5/44C10B51/00
    • C10L5/02C10B47/12C10B53/02C10L5/447C10L9/083Y02E50/10Y02E50/14Y02E50/15Y02E50/30Y02P20/145
    • A biocoke producing apparatus that realizes efficient mass production of biocoke; and a process therefor. There is disclosed a biocoke producing apparatus capable of pressure molding of a moisture-regulated pulverized biomass while heating the same in a reaction vessel (1) to thereby obtain biocoke. In the reaction vessel (1), there are preset the temperature range and pressure range for, without carbonizing of the pulverized biomass, inducing a pyrolytic or thermal curing reaction of lignin and hemicellulose thereof. The reaction vessel (1) has pressurization means for pressurizing to the pressure range, heating means for heating to the temperature range in the state of the pressurization and cooling means for cooling after maintaining of the above state. Multiple reaction vessels (1) are provided. A pulverization delivery conveyor (20) is provided superior to these reaction vessels, and each of the multiple reaction vessels is connected via a connection tube (4) to the conveyor. The connection tube (4) is provided with pulverizate charging means for charging a given amount of pulverized biomass in accordance with a timing of pulverizate charging to the reaction vessels.
    • 实现生物炭的高效批量生产的生物炭生产设备; 及其过程。 公开了一种能够在反应容器(1)中对其进行加热的同时对其进行加压成形的生物炭制造装置,从而得到生物炭素。 在反应容器(1)中,预先设定温度范围和压力范围,使得粉碎的生物质不进行碳化,引起木质素和半纤维素的热解或热固化反应。 反应容器(1)具有对压力范围进行加压的加压装置,在维持上述状态之后,加热到加热状态下的温度范围的加热装置和用于冷却的冷却装置。 提供多个反应容器(1)。 提供了优于这些反应容器的粉碎输送输送器(20),并且多个反应容器中的每一个经由连接管(4)连接到输送机。 连接管(4)设置有粉碎装料装置,用于根据向反应容器进行粉碎装料的时间对给定量的粉碎生物质进行加料。
    • 9. 发明授权
    • Apparatus and process for producing biocoke
    • 用于生产生物炭的装置和方法
    • US08454801B2
    • 2013-06-04
    • US12597603
    • 2008-04-22
    • Yoshimasa KawamiJun SatouAyumu YamazakiTamio Ida
    • Yoshimasa KawamiJun SatouAyumu YamazakiTamio Ida
    • C10B45/02
    • C10L5/44C10B47/12C10B47/28C10B53/02Y02E50/10Y02E50/14Y02E50/30Y02P20/145
    • An apparatus and process for producing biocoke usable as a substitute fuel for coal coke from biomass as a raw material. The apparatus comprises pulverizing means for pulverizing a biomass raw material attributed to photosynthesis; heating means for heating to the temperature range in which the hemicellulose of the pulverized biomass raw material is pyrolyzed so as to exhibit bonding effects; pressurization means for, in the state of the heating, pressurizing to the pressure range in which the lignin of the pulverized biomass exhibits a thermal curing reaction and maintaining the pressure; and cooling means for cooling after maintaining the state of the pressurization. The apparatus further comprises temperature detecting means provided at the exit end of the region being heated by the heating means and regulation means for judging a reaction terminal point in accordance with the result of the temperature detection and regulating the timing for transfer from heating to cooling.
    • 一种用于生产生物炭的装置和方法,其可用作煤焦油的替代燃料,其以生物质为原料。 该装置包括用于粉碎归因于光合作用的生物质原料的粉碎装置; 加热装置,其加热到粉碎的生物质原料的半纤维素被热解以显示粘合效果的温度范围; 加压装置,用于在加热状态下加压到粉碎生物质的木质素表现出热固化反应并保持压力的压力范围; 以及用于在保持加压状态之后冷却的冷却装置。 该装置还包括设置在由加热装置加热的区域的出口端处的温度检测装置和根据温度检测结果判断反应终点并调节从加热转移到冷却的时间的调节装置。