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.

公开(公告)号：US5857420A

公开(公告)日：1999-01-12

申请号：US506497

申请日：1995-07-25

Applicant: Shinroku Nishiyama

Inventor： Shinroku Nishiyama

IPC: C03B5/00 ,  C03B5/14 ,  F23G5/00 ,  F23G5/08 ,  F23G5/20 ,  F23G7/00

CPC classification number: F23G5/085 ,  C03B5/005 ,  C03B5/14 ,  F23G5/006 ,  F23G5/20 ,  F23G2201/70 ,  F23G2201/80 ,  F23G2202/104 ,  F23G2203/209 ,  F23J2215/20 ,  F23J2217/101 ,  F23J2219/60 ,  F23L2900/07005 ,  Y02E20/344 ,  Y02P40/52

Abstract: The method of an apparatus for incinerating and melting wastes along with incombustible materials in the wastes which comprise introducing wastes in a horizontal rotary furnace, incinerating the wastes at a temperature from 800.degree. C. to 1,200.degree. C., and melting the ashes of the wastes together with the remaining products which are vitrified at a temperature of more than 1,600.degree. C., by an oxygen type burner in which an oxygen-fuel mixture has an oxygen content of 50% in the mixture. The exhaust gas generated in the incineration and melting processes is introduced to a dust collector for cleaning the exhaust gas.

Abstract translation: 一种用于将废物与不可燃材料一起焚烧和熔化的设备的方法，其包括在水平旋转炉中引入废物，在800℃至1200℃的温度下对废物进行焚烧，并将废物的灰分熔化 通过其中氧气混合物在混合物中氧含量为50％的氧气型燃烧器与剩余的产品一起被浪费在1600℃以上的玻璃化温度下。 在焚烧和熔化过程中产生的废气被引入到用于净化废气的集尘器中。

公开(公告)号：US4831943A

公开(公告)日：1989-05-23

申请号：US199243

申请日：1988-05-26

Applicant: Jan A. Aune

Inventor： Jan A. Aune

IPC: B09B3/00 ,  C22B7/02 ,  F23G5/00

CPC classification number: F23G5/006 ,  B09B3/005 ,  C22B7/02 ,  F23G2201/70 ,  F23G2202/104 ,  F23G2209/30 ,  Y02P10/212

Abstract: A method of treating ash and dust from incineration plants. The ash and dush are coprocessed by mixing one or more hazardous wastes and/or metallic scraps therewith. The mixture is supplied to a smelting furnace together with a reducing agent.

公开(公告)号：WO2019001516A1

公开(公告)日：2019-01-03

申请号：PCT/CN2018/093378

申请日：2018-06-28

Applicant: 俞国豪 ,  张冬梅

Inventor： 俞国豪 ,  张冬梅

IPC: F23G7/00 ,  F23G5/30

CPC classification number: F23G5/24 ,  F23G7/001 ,  F23G2201/70 ,  F23G2209/12

Abstract: 一种湿污泥焚烧方法及流化床焚烧炉，主要解决了现有技术存在结构复杂，能耗高的问题。该湿污泥焚烧方法采用下饲式给料，在炉内不设置承压吸热受热面，而是将部分湿污泥（3）直接入炉焚烧，燃烧热量主要由湿污泥（3）的水分蒸发热、固体和含汽与燃烧烟的气体升温加以吸收，该方式既节省建造费用又减少需要干化的污泥数量，又避免了对全部湿污泥前续干化或压滤处理造成的高能耗。