-
公开(公告)号：WO2010059224A1
公开(公告)日：2010-05-27
申请号：PCT/US2009/006206
申请日：2009-11-19
Applicant: GLOBAL ENERGIES, LLC , JURANITCH, James, Charles
Inventor： JURANITCH, James, Charles
CPC classification number: C01B3/56 , C10J2300/0946 , C10J2300/1238 , C10J2300/1612 , C10J2300/1659 , C10J2300/1662 , C10J2300/1668 , C10J2300/1681 , C10J2300/1815 , C10K3/04 , Y02E50/32
Abstract: Systems and methods of generating power or producing gaseous products generate CO 2 as a waste product or as a greenhouse gas. Rather than being discharged into the atmosphere, the CO 2 is employed in a bioreactor to enhance the growth of algae. The algae then becomes a commercial product, or it can be consumed as fuel in the generation of power or the production of a gaseous product.
Abstract translation: 产生电力或生产气态产品的系统和方法产生作为废物或温室气体的二氧化碳。 而不是排入大气中，CO2被用于生物反应器以增强藻类的生长。 然后，藻类成为商业产品，或者在生成动力或生产气态产物时可以作为燃料消耗。
-
公开(公告)号：WO2010059219A1
公开(公告)日：2010-05-27
申请号：PCT/US2009/006201
申请日：2009-11-19
Applicant: GLOBAL ENERGIES, LLC , JURANITCH, James, Charles
Inventor： JURANITCH, James, Charles
CPC classification number: B01D53/62 , B01D2257/504 , B01D2259/818 , C10J2300/0946 , C10J2300/1238 , C10J2300/1612 , C10J2300/1815 , Y02C10/04 , Y02P20/152
Abstract: A method of reducing emission of greenhouse gasses, such as carbon dioxide, in a large scale process includes the steps of supplying a fuel, such as municipal waste material, to a plasma melter; supplying electrical energy to the plasma melter; supplying steam to the plasma melter; extracting a syngas from the plasma melter; providing the syngas to a heat-related process, whereby the heat-related process exhausts a greenhouse gas; and recirculating the greenhouse gas exhausted by the heat-related process to the plasma melter. Thermal energy generated by the pretreatment process is extracted and returned to the plasma melter. The plasma melter is operated in a pyrolysis mode.
Abstract translation: 在大规模工艺中减少诸如二氧化碳的温室气体排放的方法包括将诸如城市废料的燃料供应到等离子体熔化器的步骤; 向等离子体熔化器提供电能; 向等离子体熔化器供应蒸汽; 从等离子体熔化器中提取合成气; 将合成气提供给热相关过程，由此热相关过程排出温室气体; 并将通过热相关过程排出的温室气体再循环到等离子体熔化器。 由预处理过程产生的热能被提取并返回到等离子体熔化器中。 等离子体熔化器以热解模式操作。
-
公开(公告)号：WO2010002469A1
公开(公告)日：2010-01-07
申请号：PCT/US2009/003934
申请日：2009-07-01
Applicant: GLOBAL ENERGIES, LLC , JURANITCH, James, Charles
Inventor： JURANITCH, James, Charles
CPC classification number: C01B3/12 , C01B3/56 , C01B2203/0283 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C10J3/18 , C10J2300/0916 , C10J2300/093 , C10J2300/0946 , C10J2300/1238 , C10J2300/1662 , C10J2300/1671 , C10J2300/1815 , C10L3/08 , Y02E50/32 , Y02P20/145
Abstract: A system for converting carbon dioxide into a fuel to be reburned in an industrial process. The preferred feed stocks are taken from large volume carbon dioxide producers, and municipal waste. The reaction and processes reclaim lost energy in municipal waste, and industrial exhaust gas. The system is provided with a plasma melter having a feedstock input for receiving a feed fuel, and a syngas output for producing a syngas having an H 2 component. Additionally, a Sabatier reactor is provided having a hydrogen input for receiving at least a portion of the H 2 component produced by the plasma melter, and a methane output for producing CH 4 . The process has a large negative carbon footprint.
Abstract translation: 一种将二氧化碳转化为在工业过程中重新燃烧的燃料的系统。 优选的饲料来自大量二氧化碳生产者和城市垃圾。 反应和过程回收市政废物和工业废气中的能量损失。 该系统设置有具有用于接收进料燃料的原料输入的等离子体熔化器和用于产生具有H 2成分的合成气的合成气输出。 此外，提供了一种具有用于接收由等离子体熔化器产生的H 2组分的至少一部分的氢输入和用于产生CH 4的甲烷输出的Sabatier反应器。 该过程具有较大的负碳足迹。
-
公开(公告)号：WO2010059225A1
公开(公告)日：2010-05-27
申请号：PCT/US2009/006207
申请日：2009-11-19
Applicant: GLOBAL ENERGIES LLC , JURANITCH, James, Charles
Inventor： JURANITCH, James, Charles
CPC classification number: C03B5/005 , C10J2300/0946 , C10J2300/1238 , C10J2300/1612 , C10J2300/1668 , C10J2300/1815 , C10K3/04 , Y02P40/59
Abstract: A method and system for converting waste using plasma into ammonia. The method uses minimal fossil fuel, and therefore produces a minimal carbon footprint when compared to conventional processes. The method includes the steps of supplying a biomass material to a plasma melter; supplying electrical energy to the plasma melter; supplying steam to the plasma melter; extracting a syngas from the plasma melter; extracting hydrogen from the syngas; and forming ammonia from the hydrogen produced in the step of extracting hydrogen.
Abstract translation: 一种使用等离子体将废物转化为氨的方法和系统。 该方法使用最少的化石燃料，因此与常规方法相比产生最小的碳足迹。 该方法包括将生物质材料供应给等离子体熔化器的步骤; 向等离子体熔化器提供电能; 向等离子体熔化器供应蒸汽; 从等离子体熔化器中提取合成气; 从合成气中提取氢气; 并从在提取氢气的步骤中产生的氢气中形成氨。
-
公开(公告)号：WO2010065137A1
公开(公告)日：2010-06-10
申请号：PCT/US2009/006396
申请日：2009-12-04
Applicant: GLOBAL ENERGIES, LLC , JURANITCH, James, Charles
Inventor： JURANITCH, James, Charles
IPC: F23G5/00
CPC classification number: F23G5/027 , F23G5/085 , F23G2201/301 , F23G2201/303 , F23G2204/201
Abstract: A method and system for reducing emissions of greenhouse gasses during performance of a large scale industrial waste processes. The method includes the steps of supplying a waste material to a plasma melter; supplying steam to the plasma melter; extracting a syngas from the plasma melter; supplying the syngas to an industrial process; producing a waste greenhouse gas in the industrial process; returning the greenhouse gas to the plasma melter; and recycling the greenhouse gas in the plasma melter to form syngas. The waste material may be a biomass or an algae that is specifically grown from CO2 as a fuel for a plasma melter. Preferably, the plasma melter is operated in a pyrolysis mode.
Abstract translation: 在大型工业废物处理过程中减少温室气体排放的方法和系统。 该方法包括将废料供应到等离子体熔化器的步骤; 向等离子体熔化器供应蒸汽; 从等离子体熔化器中提取合成气; 将合成气供应给工业过程; 在工业过程中产生废物温室气体; 将温室气体返回到等离子熔融机; 并在等离子体熔化器中回收温室气体以形成合成气。 废料可以是从作为等离子体熔化器的燃料的二氧化碳特别生长的生物质或藻类。 优选地，等离子体熔化器以热解模式操作。
-
Patent Agency Ranking
公开(公告)号：WO2010059220A2
公开(公告)日：2010-05-27
申请号：PCT/US2009/006202
申请日：2009-11-19
Applicant: GLOBAL ENERGIES, LLC , JURANITCH, James, Charles
Inventor： JURANITCH, James, Charles
IPC: C07C1/04
CPC classification number: C01B3/56 , C01B3/12 , C07C1/04 , C10J2300/0946 , C10J2300/1238 , C10J2300/1612 , C10J2300/1815 , C10K3/04 , C10L3/08 , C07C9/04
Abstract: A method and system for converting waste using plasma into methane. The method uses minimal fossil fuel, and therefore produces a minimal carbon footprint when compared to conventional processes. The method includes the steps of supplying a biomass material to a plasma melter; supplying electrical energy to the plasma melter; supplying steam to the plasma melter; extracting a syngas from the plasma melter; extracting hydrogen from the syngas; and forming methane from the hydrogen produced in the step of extracting hydrogen.
Abstract translation: 将等离子体废物转化为甲烷的方法和系统。 该方法使用最少的化石燃料，因此与常规方法相比产生最小的碳足迹。 该方法包括将生物质材料供应给等离子体熔化器的步骤; 向等离子体熔化器提供电能; 向等离子体熔化器供应蒸汽; 从等离子体熔化器中提取合成气; 从合成气中提取氢气; 并从在提取氢气的步骤中产生的氢气中形成甲烷。
-
7.发明申请
公开(公告)号：WO2010059223A1
公开(公告)日：2010-05-27
申请号：PCT/US2009/006205
申请日：2009-11-19
Applicant: GLOBAL ENERGIES, LLC , JURANITCH, James, Charles
Inventor： JURANITCH, James, Charles
CPC classification number: C03B5/005 , C07C1/0485 , C10G2/30 , C10G2300/1003 , C10G2300/1011 , C10G2300/42 , C10G2300/807 , C10G2400/20 , C10J2300/0946 , C10J2300/1238 , C10J2300/1612 , C10J2300/1815 , C10K3/04 , Y02E50/32 , Y02P40/59 , C07C11/04
Abstract: A method and system for converting waste using plasma into ethylene. The method uses minimal fossil fuel, and therefore produces a minimal carbon footprint when compared to conventional processes. The method includes the steps of supplying a fuel material to a plasma melter; supplying electrical energy to the plasma melter; supplying steam to the plasma melter; extracting a syngas from the plasma melter; extracting hydrogen from the syngas; and forming ethylene from the hydrogen produced in the step of extracting hydrogen.
Abstract translation: 将等离子体废物转化为乙烯的方法和系统。 该方法使用最少的化石燃料，因此与常规方法相比产生最小的碳足迹。 该方法包括以下步骤：向等离子体熔化器供应燃料; 向等离子体熔化器提供电能; 向等离子体熔化器供应蒸汽; 从等离子体熔化器中提取合成气; 从合成气中提取氢气; 并从在提取氢气的步骤中产生的氢气中形成乙烯。
-
公开(公告)号：WO2010011320A1
公开(公告)日：2010-01-28
申请号：PCT/US2009/004269
申请日：2009-07-23
Applicant: GLOBAL ENERGIES, LLC , JURANITCH, James, Charles
Inventor： JURANITCH, James, Charles
IPC: C12M3/00
Abstract: A bioreactor arrangement for growing a biomass has a source of feedstock, a biomass growth surface, and a feedstock transfer arrangement that delivers the feedstock to the biomass growth surface. A biomass harvester removes the biomass from the biomass growth surface. The source of feedstock is in the form of a pool, and includes a pan for the feedstock. The biomass growth surface is configured as an absorbent belt or as a ribbed belt. A semi-permeable membrane has a porosity of approximately 30 microns, and prevents viral and sewage contamination of the biomass. The biomass growth surface is either open or closed to the atmosphere. When closed, a CO2 enhanced and temperature controlled environment is provided. Growth illumination is enhanced by a light enhancing lens or a mirror. A tracking arrangement reorients the mirror to maintain enhanced illumination on the biomass growth surface.
Abstract translation: 用于生长生物质的生物反应器装置具有原料来源，生物质生长表面和将原料输送到生物质生长生长表面的原料转移装置。 生物质收获机从生物量生长表面去除生物量。 原料来源是池的形式，包括原料的锅。 生物量生长表面被配置为吸收带或肋带。 半透膜具有约30微米的孔隙度，并防止生物质的病毒和污水污染。 生物量生长表面是开放的或关闭的大气。 关闭时，提供二氧化碳增强和温度控制的环境。 通过增光透镜或镜子增强生长照明。 跟踪装置重新定向镜子以维持生物量生长表面上的增强照明。
-
公开(公告)号：WO2012005768A1
公开(公告)日：2012-01-12
申请号：PCT/US2011/001197
申请日：2011-07-08
Applicant: JURANITCH, James, Charles , REYNOLDS, Alan, C.
Inventor： JURANITCH, James, Charles , REYNOLDS, Alan, C.
IPC: F23G5/14
CPC classification number: F22D1/003 , C10J3/18 , C10J2300/0906 , C10J2300/0946 , C10J2300/0989 , C10J2300/0996 , C10J2300/1238 , C10J2300/1606 , C10J2300/165 , C10J2300/1807 , F23G5/0276 , F23G5/033 , F23G5/085 , F23G5/16 , F23G5/46 , F23G5/50 , F23G2201/303 , F23G2202/101 , F23G2206/203 , F23G2207/30 , F23G2900/00001 , Y02E20/12 , Y02P20/129
Abstract: A method and system for converting a feedstock using thermal plasma or other gassifier, into a feedwater or make up water energy transfer system. Feedstock is any organic material or fossil fuel. The energy transferred in the feedwater or make up water is used in any Rankine or other steam process, or any process that requires heat. Heat is extracted from a gas product issued by a gassifier and is delivered to a power plant via its feedwater system or make up water system. Preferably, the gassifier is a plasma gassifier and the gas product is syngas that is combusted in an afterburner. A heated air flow and/or EGR flow is provided to the afterburner at a variable flow rate that is responsive to an operating characteristic of the afterburner.
Abstract translation: 用于使用热等离子体或其他放气器将原料转化成给水或补给水能量传递系统的方法和系统。 原料是任何有机材料或化石燃料。 在给水或补给水中转移的能量可用于任何兰金或其他蒸汽过程或任何需要加热的过程。 热气从放气器发出的气体产品中提取，并通过其给水系统或补水系统运送到发电厂。 优选地，放气器是等离子体放气器，气体产物是在加力燃烧器中燃烧的合成气。 以对响应于后燃器的操作特性的可变流量提供加热的空气流和/或EGR流。
-
公开(公告)号：WO2011002528A1
公开(公告)日：2011-01-06
申请号：PCT/US2010/001931
申请日：2010-07-02
Applicant: JURANITCH, James, Charles
Inventor： JURANITCH, James, Charles
IPC: F01N3/00
CPC classification number: C10G2/32 , C10G2300/1022 , C10G2300/42
Abstract: A system for increasing the conversion efficiency in a Fischer Tropsch based reactor system operating at low pressure for treating reactants or an exhaust stream generated by industrial processes. CO or CO 2 are sequestered and the gas is converted into a useful fuel. A plasma converter is used to generate the primary reactant which is hydrogen.
Abstract translation: 一种用于提高在低压下操作以处理反应物或由工业过程产生的废气流的基于费 - 托的反应器系统的转化效率的系统。 CO或CO 2被隔离并且气体被转化成有用的燃料。 使用等离子体转换器来产生作为氢的主要反应物。
-
-
-
-
-
-
-
-
-
Search Results
15
records
(took 0.019 seconds)
