公开(公告)号：US3972724A

公开(公告)日：1976-08-03

申请号：US561218

申请日：1975-03-24

Applicant: Karl Entzmann

Inventor： Karl Entzmann

IPC: C04B7/30 ,  F23G5/02 ,  F23G7/05 ,  C04B7/32

CPC classification number: C04B7/30 ,  F23G5/02 ,  F23G7/05 ,  F23G2201/70 ,  F23G2201/80 ,  F23G2206/203 ,  F23G2900/7013 ,  Y02E20/12 ,  Y02P40/145

Abstract: In a method of processing fuel shale to produce energy and cement clinker at the same time, oil shale and/or coal shale are disintegrated, homogenized and activated in a pin beater mill or vibrating mill. The effect of the treatment is monitored by X-ray microanalysis and the treatment is automatically controlled. The admixtures required for the production of a cement having the desired quality are added simultaneously at controlled rates. The thus treated material is then burnt in a boiler plant, preferably at combustion temperatures up to 1400.degree.C and with simultaneous sintering, whereby ash and/or slag is formed which contains at least 60% cement clinker. Said cement clinker is separated from the residual ash and slag and in an impact-type mill is disintegrated in such a manner that each clinker particle is subjected to 3-8 impacts within a time of preferably less than 0.01 second by beating elements which are moved at a velocity of at least 15 meters per second, preferably at a velocity between 50 meters and 250 meters per second.

Abstract translation: 在同时处理燃料页岩以产生能量和水泥熟料的方法中，油页岩和/或煤页岩在针刺机或振动磨中分解，均质化并活化。 通过X射线微量分析法监测治疗效果，并自动控制治疗。 生产具有所需质量的水泥所需的混合物以受控的速率同时加入。 然后将如此处理的材料在锅炉设备中燃烧，优选在高达1400℃的燃烧温度下并同时烧结，由此形成含有至少60％水泥熟料的灰分和/或炉渣。 所述水泥熟料与剩余的灰渣和炉渣分离，冲击型粉碎机以这样一种方式分解，即每个熟料颗粒在优选小于0.01秒的时间内经受3-8次冲击，通过跳动元件移动 以至少15米/秒的速度，优选以每秒50米到250米之间的速度。

公开(公告)号：US20240198306A1

公开(公告)日：2024-06-20

申请号：US18415851

申请日：2024-01-18

Applicant: SREUS ENERGY, LLC

Inventor： John Troy Kraczek ,  Gordon Ray Whipple ,  Paul James Freeman

IPC: B01J3/00 ,  C02F1/44 ,  C02F103/08 ,  F03B1/00 ,  F03B15/04 ,  F23G7/00

CPC classification number: B01J3/008 ,  C02F1/441 ,  F03B1/00 ,  F03B15/04 ,  F23G7/001 ,  B01J2219/00162 ,  C02F2103/08 ,  F05B2240/2411 ,  F23G2201/70 ,  F23G2202/30 ,  F23G2900/50003

Abstract: Fuel mixed in water is combusted in a reactor having an internal operating pressure and temperature greater than 3200 psi and greater than 374° C., where the combustion of the fuel is exothermic. Air and fuel are pressurized for introduction into the reactor to a pressure greater than the internal operating pressure using energy generated from the combustion of the fuel, and the pressurized air and the pressurized fuel are injected into the reactor. Pressurized water from the reactor is injected into a drive water column that is partially filled with water to increase a pressure of the drive water column, and water at a temperature less than 100° C. is injected into the reactor to replace water from the reactor that is injected into the drive water column. Pressurized water from the drive water column is used to drive a hydroelectric drive system to produce electrical power.

公开(公告)号：US09744575B2

公开(公告)日：2017-08-29

申请号：US14112321

申请日：2012-04-23

Applicant: David Deegan ,  Fan Zhang

Inventor： David Deegan ,  Fan Zhang

IPC: B09B3/00 ,  F23G5/08 ,  A62D3/19 ,  B09C1/06 ,  F23G5/02 ,  F23G7/14 ,  A62D101/20 ,  A62D101/22 ,  A62D101/28

CPC classification number: B09B3/00 ,  A62D3/19 ,  A62D2101/20 ,  A62D2101/22 ,  A62D2101/28 ,  B09C1/06 ,  F23G5/02 ,  F23G5/085 ,  F23G7/14 ,  F23G2201/70 ,  F23G2900/50212 ,  F23G2900/7007 ,  F23G2900/7011 ,  Y02W10/40

Abstract: A method for the treatment of waste by plasma treating the waste to destroy the hazardous organic components and to yield a slag and an off-gas by plasma treating the waste in the presence of added oxygen gas in a transferred-arc plasma treatment unit, followed by directing off-gas from the plasma treatment unit to a thermal oxidizer combustion chamber.

公开(公告)号：US20140364674A1

公开(公告)日：2014-12-11

申请号：US14300494

申请日：2014-06-10

Applicant: Robert Toby Wilson ,  Tommy S. Cheng

Inventor： Robert Toby Wilson ,  Tommy S. Cheng

IPC: F23G5/02 ,  B09B3/00 ,  F23G7/00

CPC classification number: F23G5/02 ,  B09B3/0008 ,  B09B3/0075 ,  F23G7/008 ,  F23G2201/70 ,  F23G2209/20

Abstract: Methods and products for cleanup of fluid medical waste. In one illustrative embodiment, a product may include coconut coir in a loose granulated grade, a compressed pellet grade, or mixture thereof allowing users to choose between grades more ideal for their application while achieving the same results of absorbing and solidifying all human waste and fluids for safe removal and disposal. In a second illustrative embodiment, a product may include coir in a proportion of from about 85% to about 99% and a suitable microbe for initiating bioremediation in an appropriate form in a proportion of from about 20% to about 1%, by weight.

Abstract translation: 流体医疗废物清理方法和产品。 在一个说明性的实施方案中，产品可以包括松散颗粒级的椰子椰子，压缩颗粒级或其混合物，允许用户在其应用之间选择更理想，同时实现相同的结果吸收和固化所有人类废物和流体 用于安全清除和处置。 在第二说明性实施方案中，产品可以包括约85％至约99％的比例的椰子和用于以按重量计约20％至约1％的比例以适当形式引发生物修复的合适的微生物。

公开(公告)号：US08015932B2

公开(公告)日：2011-09-13

申请号：US11950615

申请日：2007-12-05

Applicant: Boris Nikolaevich Eiteneer ,  William Randall Seeker ,  Roy Payne

Inventor： Boris Nikolaevich Eiteneer ,  William Randall Seeker ,  Roy Payne

IPC: F23C1/10 ,  F23K3/02 ,  F23N5/02 ,  F23D1/00

CPC classification number: F23C1/00 ,  F23C2201/301 ,  F23C2900/01001 ,  F23G2201/70

Abstract: A fuel flexible furnace, including a main combustion zone, a reburn zone downstream from the main combustion zone, and a delivery system operably coupled to supplies of biomass and coal and configured to deliver the biomass and the coal as ingredients of first and reburn fuels to the main combustion zone and the reburn zone, with each fuel including flexible quantities of the biomass and/or the coal. The flexible quantities are variable with the furnace in an operating condition.

Abstract translation: 一种燃料柔性炉，包括主燃烧区，在主燃烧区下游的重燃区，以及可操作地耦合到生物质和煤的供应并被配置为将生物质和煤作为第一和再燃燃料的成分输送的输送系统， 主燃烧区和重燃区，每个燃料包括生物量和/或煤的灵活数量。 炉子在运行状态下的灵活数量是可变的。

公开(公告)号：US20070266916A1

公开(公告)日：2007-11-22

申请号：US11832293

申请日：2007-08-01

Applicant: Brian Copeland ,  Gregory Coil ,  Robert Latta ,  Thomas Lenaghan

Inventor： Brian Copeland ,  Gregory Coil ,  Robert Latta ,  Thomas Lenaghan

IPC: F23G5/30 ,  F23G5/04 ,  F23J3/00

CPC classification number: F23G7/10 ,  F23C10/30 ,  F23G5/04 ,  F23G5/12 ,  F23G5/30 ,  F23G5/46 ,  F23G2201/70 ,  F23G2206/203 ,  F23J7/00 ,  F23J15/025 ,  F23J2215/20 ,  F23J2217/101 ,  Y02E20/12

Abstract: A process comprising, providing an agricultural biofuel to a fluidized bed reactor and combusting the agricultural biofuel to produce heat and/or steam is disclosed. In one embodiment systems for generating energy with agricultural biofuel are provided. In one embodiment, the agricultural biofuel is selected from the group consisting of agricultural crops, crop residues, grain processing facility waste, value-added agricultural facility byproducts, livestock production facility waste, livestock processing facility waste and food processing facility waste. In one embodiment, the heat and/or steam is used to generate electricity. In other embodiments, the heat and/or steam is used to power the grain processing facility, livestock production facility, livestock processing facility or food processing facility. In another embodiment, one or more environmental controls are used. In a particular embodiment, ethanol byproducts are used as the agricultural biofuel.

Abstract translation: 公开了一种方法，其包括向流化床反应器提供农业生物燃料并燃烧农业生物燃料以产生热量和/或蒸汽。 在一个实施例中，提供了用农业生物燃料产生能量的系统。 在一个实施方案中，农业生物燃料选自农作物，作物残余物，谷物加工设备废物，增值农业设备副产品，牲畜生产设备废物，牲畜加工设备废物和食品加工设备废物。 在一个实施例中，热和/或蒸汽用于发电。 在其他实施例中，使用热和/或蒸汽为谷物加工设备，牲畜生产设备，牲畜加工设备或食品加工设备供电。 在另一个实施例中，使用一个或多个环境控制。 在一个具体的实施方案中，乙醇副产物用作农业生物燃料。

公开(公告)号：US20050274308A1

公开(公告)日：2005-12-15

申请号：US10373668

申请日：2003-02-24

Applicant: Brian Copeland ,  Gregory Coil ,  Robert Latta ,  Thomas Lenaghan

Inventor： Brian Copeland ,  Gregory Coil ,  Robert Latta ,  Thomas Lenaghan

IPC: F23C10/30 ,  F23G1/00 ,  F23G5/04 ,  F23G5/12 ,  F23G5/30 ,  F23G5/46 ,  F23G7/10 ,  F23J7/00 ,  F23J15/02 ,  F23B7/00

CPC classification number: F23G7/10 ,  F23C10/30 ,  F23G5/04 ,  F23G5/12 ,  F23G5/30 ,  F23G5/46 ,  F23G2201/70 ,  F23G2206/203 ,  F23J7/00 ,  F23J15/025 ,  F23J2215/20 ,  F23J2217/101 ,  Y02E20/12

Abstract: A process comprising, providing an agricultural biofuel to a fluidized bed reactor and combusting the agricultural biofuel to produce heat and/or steam is disclosed. In one embodiment, the agricultural biofuel is selected from the group consisting of agricultural crops, crop residues, grain processing facility waste, value-added agricultural facility byproducts, livestock production facility waste, livestock processing facility waste and food processing facility waste. In one embodiment, the heat and/or steam is used to generate electricity. In other embodiments, the heat and/or steam is used to power the grain processing facility, livestock production facility, livestock processing facility or food processing facility. In another embodiment, one or more environmental controls are used. In a particular embodiment, ethanol byproducts are used as the agricultural biofuel.

Abstract translation: 公开了一种方法，其包括向流化床反应器提供农业生物燃料并燃烧农业生物燃料以产生热量和/或蒸汽。 在一个实施方案中，农业生物燃料选自农作物，作物残余物，谷物加工设备废物，增值农业设备副产品，牲畜生产设备废物，牲畜加工设备废物和食品加工设备废物。 在一个实施例中，热和/或蒸汽用于发电。 在其他实施例中，使用热和/或蒸汽为谷物加工设备，牲畜生产设备，牲畜加工设备或食品加工设备供电。 在另一个实施例中，使用一个或多个环境控制。 在一个具体的实施方案中，乙醇副产物用作农业生物燃料。

公开(公告)号：US20020068846A1

公开(公告)日：2002-06-06

申请号：US09840094

申请日：2001-04-24

Applicant: SAN IKU CO., LTD.

Inventor： Hisao Tsuruta

IPC: A62D003/00 ,  F23C001/10 ,  F23C001/12 ,  F23B007/00

CPC classification number: F23G5/12 ,  F23G7/001 ,  F23G7/065 ,  F23G7/12 ,  F23G7/14 ,  F23G2201/70 ,  F23G2209/20 ,  F23G2900/00001 ,  Y10S588/90

Abstract: A method for making harmless a material to be treated containing a pollutant, including the steps of arranging a pair of ejecting nozzles such that nozzle openings thereof are opposed to each other inside a pressure-proof furnace, thermally treating that material, ejecting the thermally treated material through each of the nozzle openings of the nozzles, respectively, and colliding the material ejected through one of the nozzles with that ejected through the other in a space inside the pressure-proof furnace and between a pair of the nozzle openings such that a portion of the pollutant of the material remaining non-decomposed by the thermal treatment may be decomposed.

Abstract translation: 一种使含有污染物的待处理材料无害化的方法，包括以下步骤：在耐压炉内设置一对喷嘴，使其喷嘴开口彼此相对，热处理该材料，喷射热处理 分别通过喷嘴的每个喷嘴开口的材料，并且通过一个喷嘴喷射的材料与在耐压炉内部的空间和一对喷嘴开口之间的另一个喷射的材料相撞，使得一部分 的通过热处理而未分解的材料的污染物可能被分解。

公开(公告)号：US06301896B1

公开(公告)日：2001-10-16

申请号：US09379903

申请日：1999-08-24

Applicant: Norihisa Miyoshi ,  Shosaku Fujinami ,  Tetsuhisa Hirose ,  Masaaki Irie ,  Kazuo Takano ,  Takahiro Oshita

Inventor： Norihisa Miyoshi ,  Shosaku Fujinami ,  Tetsuhisa Hirose ,  Masaaki Irie ,  Kazuo Takano ,  Takahiro Oshita

IPC: F01K100

CPC classification number: F23G5/006 ,  F01K23/067 ,  F22B31/045 ,  F23G5/027 ,  F23G5/46 ,  F23G5/48 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2201/70 ,  F23G2202/103 ,  F23G2202/20 ,  F23G2203/30 ,  F23J15/025 ,  F23J2215/30 ,  F23J2217/104 ,  F23J2219/10 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18

Abstract: In an improved system for recovering heat from a combustion gas produced by burning wastes, the combustion gas or combustible gas produced by partial burning of the wastes subjected to dust filtration in a temperature range of 450-650° C. at a filtration velocity of 1-5 cm/sec under a pressure of from −5 kPa (gage) to 5 MPa before heat recovery is effected. The dust filtration is preferably performed using a filter medium which may or may not support a denitration catalyst. Heat recovery is preferably effected using a steam superheater. The dust-free gas may partly or wholly be reburnt with or without an auxiliary fuel to a sufficiently high temperature to permit heat recovery. The combustion furnace may be a gasifying furnace which, in turn, may be combined with a melting furnace. If desired, the reburning to a higher temperature may be performed under pressure and the obtained hot combustion gas is supplied to a gas turbine to generate electricity, followed by introduction of the exhaust gas from the gas turbine into a steam superheater for further heat recovery. The system can raise the temperature of superheated steam to a sufficient level to enhance the efficiency of power generation without possibility of corrosion of heat transfer pipes by the combustion gas or combustible gas.

Abstract translation: 在用于从燃烧废物产生的燃烧气体中回收热量的改进系统中，通过在过滤速度为1的450-650℃的温度范围内进行灰尘过滤的部分燃烧部分燃烧产生的燃烧气体或可燃气体 -5厘米/秒，压力为-5千帕（表压）至5MPa。 灰尘过滤优选使用可以或可以不支持脱硝催化剂的过滤介质进行。 热回收优选使用蒸汽过热器进行。 无尘气体可以部分或全部地被反燃，有或没有辅助燃料到足够高的温度以允许热回收。 燃烧炉可以是气化炉，其又可以与熔炉组合。 如果需要，可以在压力下进行再燃烧到更高的温度，并且将获得的热燃烧气体供应到燃气轮机以产生电力，然后将来自燃气轮机的废气引入蒸汽过热器中以进一步热回收。 该系统可以将过热蒸汽的温度升高到足够的水平，以提高发电效率，而不会由燃烧气体或可燃气体导致传热管的腐蚀。

公开(公告)号：US06298666B1

公开(公告)日：2001-10-09

申请号：US09379591

申请日：1999-08-24

Applicant: Norihisa Miyoshi ,  Shosaku Fujinami ,  Tetsuhisa Hirose ,  Masaaki Irie ,  Kazuo Takano ,  Takahiro Oshita

Inventor： Norihisa Miyoshi ,  Shosaku Fujinami ,  Tetsuhisa Hirose ,  Masaaki Irie ,  Kazuo Takano ,  Takahiro Oshita

IPC: F01K100

CPC classification number: F23G5/006 ,  F01K23/067 ,  F22B31/045 ,  F23G5/027 ,  F23G5/46 ,  F23G5/48 ,  F23G2201/303 ,  F23G2201/304 ,  F23G2201/40 ,  F23G2201/70 ,  F23G2202/103 ,  F23G2202/20 ,  F23G2203/30 ,  F23J15/025 ,  F23J2215/30 ,  F23J2217/104 ,  F23J2219/10 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18

Abstract: In an improved system for recovering heat from a combustion gas produced by burning wastes, the combustion gas or combustible gas produced by partial burning of the wastes subjected to dust filtration in a temperature range of 450-650° C. at a filtration velocity of 1-5 cm/sec under a pressure of from −5 kPa (gage) to 5 MPa before heat recovery is effected. The dust filtration is preferably performed using a filter medium which may or may not support a denitration catalyst. Heat recovery is preferably effected using a steam superheater. The dust-free gas may partly or wholly be reburnt with or without an auxiliary fuel to a sufficiently high temperature to permit heat recovery. The combustion furnace may be a gasifying furnace which, in turn, may be combined with a melting furnace. If desired, the reburning to a higher temperature may be performed under pressure and the obtained hot combustion gas is supplied to a gas turbine to generate electricity, followed by introduction of the exhaust gas from the gas turbine into a steam superheater for further heat recovery. The system can raise the temperature of superheated steam to a sufficient level to enhance the efficiency of power generation without possibility of corrosion of heat transfer pipes by the combustion gas or combustible gas.