公开(公告)号：US11982444B2

公开(公告)日：2024-05-14

申请号：US17463623

申请日：2021-09-01

Applicant: GUANGDONG UNIVERSITY OF TECHNOLOGY ,  Guangzhou Herui Energy Conservation and Environmental Protection Technology Co., Ltd.

Inventor： Xiaozhou Liu ,  Peibin Lin ,  Guangyu Zhu ,  Wei Liu ,  Yu Zhang

IPC: F23G5/04 ,  F23G5/12 ,  F23G5/44 ,  F23G5/46 ,  F23G7/00

CPC classification number: F23G5/04 ,  F23G5/12 ,  F23G5/442 ,  F23G5/46 ,  F23G7/001 ,  F23G2201/10 ,  F23G2201/20 ,  F23G2205/122 ,  F23G2206/10

Abstract: A system for disposing a high-moisture mixed waste composed of kitchen garbage and water-containing sludge is provided, including a mixed waste storage device, a mixed waste primary-drying device and a mixed waste incinerating device. The mixed waste primary-drying device includes a mixed waste primary-drying body, a primary-drying material inlet, a primary-dried material outlet, a drying gas inlet and a primary waste gas outlet. A discharging outlet of the mixed waste storage device is connected with the primary-drying material inlet through the first conveying belt. The mixed waste incinerating device includes an incinerator, an incineration material inlet, an incineration material outlet, a combustion-supporting gas inlet and a flue gas outlet. The incineration material inlet is connected with the primary-dried material outlet through the second conveying belt and the combustion-supporting gas inlet is connected with the primary waste gas outlet. The flue gas outlet is connected with the drying gas inlet.

公开(公告)号：US11965651B2

公开(公告)日：2024-04-23

申请号：US17280182

申请日：2019-09-25

Applicant: Jorge Luis Osório Carvalho

Inventor： Jorge Cortizo Carvalho

IPC: F23G5/04 ,  B65G69/20 ,  F26B3/04 ,  F26B23/02

CPC classification number: F23G5/04 ,  B65G69/20 ,  F26B3/04 ,  F26B23/028 ,  F23G2201/10 ,  F23G2201/60 ,  F23G2201/90 ,  F23G2206/10 ,  F23G2207/101 ,  F23N2225/10 ,  F26B2200/02

Abstract: The continuous process of the present invention is intended to obtain dry biomass from two treatment steps by drying organic waste. The waste previously sieved and crushed waste are dumped into a first dryer, inside of which temperatures are between 280° C. and 300° C. at the inlet thereof and between 90° C. and 100° C. at the outlet, then passing to a conveyor belt where at room temperature a partial cool-down occurs and the waste is dumped into a second dryer inside of which the temperatures are between 180° C. and 200° C. at the inlet and between 75° C. and 85° C. at the exit, completing the process, during which the interior of the dryers is maintained in negative pressure through exhaust flow and the oxygen content is kept between 5 and 7%.

公开(公告)号：US20170234529A1

公开(公告)日：2017-08-17

申请号：US15444193

申请日：2017-02-27

Applicant: Daniel R. Higgins ,  Eugene Sullivan

Inventor： Daniel R. Higgins ,  Eugene Sullivan

IPC: F22G5/02 ,  F23C9/00 ,  F23G5/00 ,  F23G5/04 ,  F23G5/05 ,  F23G7/10 ,  F23J1/00 ,  F23K3/00 ,  F23L7/00 ,  F22B21/14 ,  F22G1/04 ,  F23G5/24

CPC classification number: F22G5/02 ,  F22B21/00 ,  F22B21/14 ,  F22G1/04 ,  F23C9/00 ,  F23C9/006 ,  F23C2900/01001 ,  F23G5/002 ,  F23G5/04 ,  F23G5/05 ,  F23G5/24 ,  F23G5/46 ,  F23G7/00 ,  F23G7/10 ,  F23G2202/106 ,  F23G2205/16 ,  F23G2206/10 ,  F23H13/06 ,  F23J1/00 ,  F23K3/00 ,  F23L7/007 ,  F23M3/22 ,  Y02E20/12 ,  Y02E20/344

Abstract: A ground supported single drum power boiler is described combining a refractory lined and insulated V-Cell floor; refractory lined and insulated combustion chamber; integrated fuel chutes configured to pre-dry wet solid fuel; top mounted fuel bin; internal chamber walls; configurable combustion air systems; and a back pass with after-burner ports and cross flow superheaters. The boiler can be configured in pre-assembled modules to minimize the field construction time and cost. An alternative embodiment is adaptable as a gasifier.

公开(公告)号：US20170227215A1

公开(公告)日：2017-08-10

申请号：US15494572

申请日：2017-04-24

Applicant: ZHONGYING CHANGJIANG INTERNATIONAL NEW ENERGY INVESTMENT CO., LTD.

Inventor： Yilong CHEN ,  Shuchuan HU ,  Yanfeng ZHANG

IPC: F23G5/04 ,  F23G5/46 ,  F23G5/44

CPC classification number: F23G5/04 ,  F23G5/444 ,  F23G5/46 ,  F23G2201/101 ,  F23G2205/122 ,  F23G2206/10 ,  F23K2201/20 ,  F26B15/18 ,  F26B17/02 ,  F26B17/08 ,  F26B21/14 ,  F26B23/001 ,  F26B2200/02 ,  Y02P70/40 ,  Y02P70/405

Abstract: A method for drying biomass fuel using waste heat of flue gas from a power plant. The method includes: 1) stepwise recovering, by multi-stage condensation, sensible heat of flue gas; stepwise heating air using the sensible heat, to yield first-stage dry air and second-stage dry air; 2) convectively drying and dehydrating biomass fuel using the first-stage dry air having a temperature of between 150 and 180° C.; 3) further convectively drying and dehydrating the biomass fuel using the second-stage dry air having a temperature of between 80 and 100° C.; and 4) drying and dehydrating the biomass fuel using the third-stage dry air having a temperature of less than or equal to 25° C.

公开(公告)号：US09657989B2

公开(公告)日：2017-05-23

申请号：US13452678

申请日：2012-04-20

Applicant: Bruce Johnson ,  Nina Cunningham ,  Michael C. Mensinger

Inventor： Bruce Johnson ,  Nina Cunningham ,  Michael C. Mensinger

IPC: F26B23/02 ,  F23G5/027 ,  F23G5/04 ,  F23G5/16

CPC classification number: F26B23/028 ,  F23G5/027 ,  F23G5/04 ,  F23G5/16 ,  F26B2200/18 ,  Y02E20/12 ,  Y02P80/21

Abstract: The present invention relates to methods and systems for processing sewage sludge using a gasification process. The gasification process takes place at high temperatures in an oxygen-starved environment, which enables carbon-containing materials in the sewage sludge to chemically react under the preferred temperature and oxygen levels, resulting in the formation of usable products, including ash, electricity, and syngas—all of which are generally environmentally benign.

公开(公告)号：US09574147B2

公开(公告)日：2017-02-21

申请号：US14289258

申请日：2014-05-28

Applicant: RES USA, LLC

Inventor： Randy Blevins ,  Joshua B. Pearson ,  Harold A. Wright

IPC: C10J3/30 ,  C10J3/80 ,  F23G5/04 ,  C10J3/48 ,  B01J8/06 ,  B01J19/24 ,  F23G5/033 ,  F23G5/44 ,  C01B3/34 ,  C10G2/00

CPC classification number: C10J3/466 ,  B01J8/067 ,  B01J19/2415 ,  B01J19/242 ,  B01J19/2425 ,  B01J19/243 ,  B01J2208/00309 ,  B01J2208/00504 ,  B01J2219/00006 ,  B01J2219/00157 ,  B01J2219/00159 ,  B01J2219/24 ,  C01B3/02 ,  C01B3/346 ,  C01B2203/0216 ,  C01B2203/0811 ,  C01B2203/1241 ,  C10G2/30 ,  C10G2/34 ,  C10J3/30 ,  C10J3/485 ,  C10J3/80 ,  C10J2200/09 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/0976 ,  C10J2300/1223 ,  C10J2300/1246 ,  C10J2300/1659 ,  C10J2300/1687 ,  C10J2300/1853 ,  F23G5/033 ,  F23G5/04 ,  F23G5/444 ,  Y02E50/32 ,  Y02P20/145

Abstract: A mixing apparatus for producing a feedstock for a reformer, the mixing apparatus including at least one mixing vessel comprising a cylindrical vessel with a conical bottom; a steam inlet configured for introducing steam into the conical bottom; a carbonaceous material inlet configured for introducing a carbonaceous feed into the cylindrical vessel; and an outlet for a reformer feedstock comprising at least 0.3 pounds of steam per pound of carbonaceous material, with the at least one mixing vessel configured for operation at a pressure of greater than about 10 psig.

Abstract translation: 一种用于生产用于重整器的原料的混合装置，所述混合装置包括至少一个混合容器，所述混合容器包括具有锥形底部的圆柱形容器; 蒸汽入口，构造成将蒸汽引入锥形底部; 碳质材料入口，构造成用于将碳质进料引入到圆柱形容器中; 以及重整器原料的出口，其包含每磅碳质材料至少0.3磅的蒸汽，所述至少一个混合容器构造成在大于约10psig的压力下操作。

公开(公告)号：US09453677B2

公开(公告)日：2016-09-27

申请号：US14269551

申请日：2014-05-05

Applicant: Holcim Technology Ltd

Inventor： Urs Gasser

IPC: F26B21/06 ,  F26B23/00 ,  F23G5/46 ,  F23G5/04 ,  F23G7/00 ,  C04B7/44 ,  F26B23/02 ,  F27B7/20 ,  F27D17/00 ,  F26B11/02 ,  F26B3/02

CPC classification number: F26B23/002 ,  C04B7/4407 ,  C04B7/4423 ,  F23G5/04 ,  F23G5/46 ,  F23G7/001 ,  F23G2206/10 ,  F23G2206/201 ,  F23G2900/50211 ,  F26B3/02 ,  F26B11/024 ,  F26B23/028 ,  F26B2200/18 ,  F27B7/2025 ,  F27B7/2033 ,  F27D17/004 ,  F27D17/008 ,  Y02E20/363 ,  Y02P40/126

Abstract: In a method for reprocessing wet waste materials containing organic components, in particular sludges in a cement clinker production plant, in which raw meal is preheated in a preheater (3) in countercurrent flow to the hot exhaust gases of a clinker furnace (2), and calcined in a calciner (4) fired with alternative fuels, the wet waste materials are dried in a drying unit (18) using a hot gas produced from the preheater waste heat and the dried waste materials and the drier exhaust gases are discharged from the drying unit (18), wherein the drier exhaust gases are introduced into the calciner (4).

公开(公告)号：US20160229811A1

公开(公告)日：2016-08-11

申请号：US15023159

申请日：2014-09-25

Applicant: THE BOARD OF TRUSTEES OF THE UNIVERSITY OF ILLINOIS ,  DUKE UNIVERSITY

Inventor： John Katzenelienbogen ,  Donald McDonneli ,  John D, Norris ,  Alexander Parent ,  Julie Pollock ,  Jillian Gunther ,  Kathryn E. Carlson ,  Teresa Martin

IPC: C07D239/48 ,  C07D239/47 ,  C07D213/74 ,  C07D401/14 ,  C07D403/14 ,  C07D239/52 ,  C07D239/54 ,  C07D407/08 ,  C07D239/26 ,  C07D239/58 ,  C07D239/30 ,  C07D213/24 ,  C07D241/12 ,  C07D241/16 ,  C07D409/14 ,  C07D239/34 ,  C07D241/18 ,  C07D403/08

CPC classification number: C07D239/48 ,  A61K45/06 ,  C07D213/24 ,  C07D213/74 ,  C07D239/26 ,  C07D239/30 ,  C07D239/34 ,  C07D239/47 ,  C07D239/52 ,  C07D239/54 ,  C07D239/58 ,  C07D241/12 ,  C07D241/16 ,  C07D241/18 ,  C07D401/14 ,  C07D403/08 ,  C07D403/14 ,  C07D407/08 ,  C07D409/08 ,  C07D409/14 ,  F01K5/02 ,  F23G5/04 ,  F23K1/04 ,  F23K3/00 ,  F23K2201/20 ,  F23K2203/103

Abstract: The present disclosure provides tetra-substituted cyclobutane inhibitors of Androgen Receptor Action, and methods of using such inhibitors, for the treatment of hormone-refractory cancers.

Abstract translation: 本公开提供了雄激素受体作用的四取代环丁烷抑制剂以及使用这些抑制剂用于治疗激素难治性癌症的方法。

公开(公告)号：US09360211B2

公开(公告)日：2016-06-07

申请号：US13613635

申请日：2012-09-13

Applicant: Satoru Sugita ,  Shintaro Honjo ,  Takuya Okamoto

Inventor： Satoru Sugita ,  Shintaro Honjo ,  Takuya Okamoto

IPC: F23G5/04 ,  F23L15/04 ,  F23J15/02 ,  F23J15/04 ,  F23K1/04

CPC classification number: F23G5/04 ,  B03C3/017 ,  F23J15/022 ,  F23J15/04 ,  F23J2217/102 ,  F23K1/04 ,  F23K2201/10 ,  F23K2201/20 ,  F23L15/04 ,  Y02E20/348 ,  Y02P80/152

Abstract: Coal is properly dried and the efficiency of a boiler is increased while suppressing any reduction in efficiency of the boiler and the generation of hydrocarbon gas components. Employed are a coal dryer that dries coal, a boiler in which the coal that is dried in the coal dryer is mixed with air for combustion and burned, an air heater that heats the air for combustion that is supplied to the boiler using combustion exhaust gas discharged from the boiler, a precipitator that collects dust included in the combustion exhaust gas, a desulfurization plant that performs a desulfurization process on the combustion exhaust gas, and heat recovery equipment that heats a heating medium using the combustion exhaust gas. The coal dryer dries the coal using the heat energy of the heating medium that has been heated in the heat recovery equipment.

Abstract translation: 煤被适当地干燥并且锅炉的效率增加，同时抑制了锅炉的效率的降低和烃气体成分的产生。 使用干燥煤的煤干燥器，将在煤干燥机中干燥的煤与燃烧和燃烧的空气混合的锅炉，使用燃烧废气加热供给锅炉的空气进行燃烧的空气加热器 从锅炉排出的除尘器，收集燃烧废气中的灰尘的除尘器，对燃烧废气进行脱硫处理的脱硫装置，以及使用燃烧废气加热加热介质的热回收装置。 煤干燥机使用在热回收设备中加热的加热介质的热能来干燥煤。

公开(公告)号：US09273904B2

公开(公告)日：2016-03-01

申请号：US14354028

申请日：2012-10-18

Applicant: Holcim Technology Ltd

Inventor： Urs Gasser

IPC: F26B23/00 ,  F23G5/46 ,  F23G5/04 ,  F23G7/00 ,  C04B7/44 ,  F26B23/02 ,  F27B7/20 ,  F27D17/00 ,  F26B11/02 ,  F26B3/02

CPC classification number: F26B23/002 ,  C04B7/4407 ,  C04B7/4423 ,  F23G5/04 ,  F23G5/46 ,  F23G7/001 ,  F23G2206/10 ,  F23G2206/201 ,  F23G2900/50211 ,  F26B3/02 ,  F26B11/024 ,  F26B23/028 ,  F26B2200/18 ,  F27B7/2025 ,  F27B7/2033 ,  F27D17/004 ,  F27D17/008 ,  Y02E20/363 ,  Y02P40/126

Abstract: In a method for reprocessing wet waste materials containing organic components, in particular sludges in a cement clinker production plant, in which raw meal is preheated in a preheater (3) in countercurrent flow to the hot exhaust gases of a clinker furnace (2), and calcined in a calciner (4) fired with alternative fuels, the wet waste materials are dried in a drying unit (18) using a hot gas produced from the preheater waste heat and the dried waste materials and the drier exhaust gases are discharged from the drying unit (18), wherein the drier exhaust gases are introduced into the calciner (4).