US20070210075A1 - Induction heater - Google Patents

Induction heater Download PDF

Info

Publication number
US20070210075A1
US20070210075A1 US11/713,142 US71314207A US2007210075A1 US 20070210075 A1 US20070210075 A1 US 20070210075A1 US 71314207 A US71314207 A US 71314207A US 2007210075 A1 US2007210075 A1 US 2007210075A1
Authority
US
United States
Prior art keywords
enclosure
heating system
heating
thermal transmitter
induction coil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US11/713,142
Other languages
English (en)
Inventor
John Self
Robert Olexy
Steve Cochran
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shaw Intellectual Property Holdings Inc
Original Assignee
SHAW WASTE SOLUTIONS LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SHAW WASTE SOLUTIONS LLC filed Critical SHAW WASTE SOLUTIONS LLC
Priority to US11/713,142 priority Critical patent/US20070210075A1/en
Assigned to SHAW WASTE SOLUTIONS, LLC reassignment SHAW WASTE SOLUTIONS, LLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: OLEXY, ROBERT A., SELF, JOHN, COCHRAN, STEVE
Publication of US20070210075A1 publication Critical patent/US20070210075A1/en
Assigned to SHAW INTELLECTUAL PROPERTY HOLDINGS, INC. reassignment SHAW INTELLECTUAL PROPERTY HOLDINGS, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SWS HOLDINGS, LLC
Assigned to SWS HOLDINGS, LLC reassignment SWS HOLDINGS, LLC CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: SHAW WASTE SOLUTIONS, LLC
Abandoned legal-status Critical Current

Links

Images

Classifications

    • H—ELECTRICITY
    • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
    • H05B6/00—Heating by electric, magnetic or electromagnetic fields
    • H05B6/02—Induction heating
    • H05B6/10—Induction heating apparatus, other than furnaces, for specific applications
    • H05B6/105—Induction heating apparatus, other than furnaces, for specific applications using a susceptor
    • H05B6/108—Induction heating apparatus, other than furnaces, for specific applications using a susceptor for heating a fluid
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
    • C10J3/60—Processes
    • C10J3/64—Processes with decomposition of the distillation products
    • C10J3/66—Processes with decomposition of the distillation products by introducing them into the gasification zone
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • C10K3/001—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by thermal treatment
    • C10K3/003—Reducing the tar content
    • C10K3/006—Reducing the tar content by steam reforming
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0211—Processes for making hydrogen or synthesis gas containing a reforming step containing a non-catalytic reforming step
    • C01B2203/0216—Processes for making hydrogen or synthesis gas containing a reforming step containing a non-catalytic reforming step containing a non-catalytic steam reforming step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/06—Integration with other chemical processes
    • C01B2203/066—Integration with other chemical processes with fuel cells
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
    • C01B2203/0855—Methods of heating the process for making hydrogen or synthesis gas by electromagnetic heating
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/80—Aspect of integrated processes for the production of hydrogen or synthesis gas not covered by groups C01B2203/02 - C01B2203/1695
    • C01B2203/84—Energy production
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00—Details of gasification apparatus
    • C10J2200/15—Details of feeding means
    • C10J2200/158—Screws
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/0916—Biomass
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0973—Water
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
    • C10J2300/1861—Heat exchange between at least two process streams
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
    • C10J2300/1861—Heat exchange between at least two process streams
    • C10J2300/1884—Heat exchange between at least two process streams with one stream being synthesis gas
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock
    • Y02P20/145—Feedstock the feedstock being materials of biological origin

Definitions

  • the present invention relates to a method and apparatus for heating fluids, particularly to a method and apparatus for heating fluids by way of induction heating.
  • Fluid heating systems are employed in the domestic, commercial, and industrial heating of fluids.
  • batch heated systems i.e. Fluid-tank heaters
  • continuous heated systems i.e. tankless fluid heaters
  • Both of these heating systems may be electrically heated and/or they may be gas-fired heated.
  • these fluid heating systems can be inefficient, costly, and may not produce an effective residence time when heating the fluid.
  • the present invention is directed to a system and method for heating fluids in which induction heating is employed in an efficient manner to heat a fluid.
  • the heating of fluids by way of induction heating can result in the effective and rapid heating of fluids which can be very advantageous for many fluid heating applications.
  • the induction fluid heating system comprises:
  • At least one power supply for supplying current to said at least one induction coil to heat said thermal transmitter wherein said heating system is used for heating fluids.
  • FIG. 1 is a schematic diagram of a preferred embodiment of the present invention.
  • the present invention relates to a system and method for heating fluids in which induction heating is employed in an efficient manner to provide for an effective fluid heater.
  • Fluid is herein defined as one or more substances, as a liquid or gas, that is capable of flowing and that changes its shape at a steady rate when acted upon by a force tending to change its shape.
  • FIG. 1 illustrates a preferred embodiment of the present invention.
  • inductively heated system 50 is used for heating fluids to a desired temperature.
  • the desired temperature will be dependent on the type of operation is which the heating system is used.
  • the design of the heating system can be modified to be used in almost any system in which fluids are heated.
  • the preferred embodiment of the heating system 50 depicted in FIG. 1 shows an enclosure 51 , thermal transmitters 52 , induction coil 53 , and filter 55 .
  • the filter on this heating system is optional.
  • the fields of use of the design depicted in FIG. 1 can include any uses or operations wherein it is desired to heat a fluid stream to a desired temperature.
  • this technology can be utilized in such applications that include but are not limited to, an on-demand hot water heater for personal or industrial use, a steam generator, a pre-heater, a heat exchanger, a scrubber or absorption unit, a reactor or any like device wherein it is desired to efficiently and quickly heat a fluid.
  • enclosure 51 would be made of a substantially non-electrically conductive material.
  • enclosure 51 is substantially made of a ceramic material or a composite thereof.
  • Enclosure 51 is preferably at least partially surrounded by at least one induction coil 53 whereby induction heating is employed to heat a fluid to a desired temperature.
  • the desired material used to build the enclosure will be substantially invisible to the electromagnetic energy generated by the induction coil 53 so that the electromagnetic energy may penetrate the enclosure to heat the thermal transmitters 52 discussed below in more detail.
  • enclosure 51 is filled with thermal transmitters 52 which include, but are not limited to, geometric structures substantially made of a material that has a high electrical resistivity, a high melting point, and a thermal conductivity.
  • Thermal transmitters 52 receive electromagnetic energy from induction coil 53 which preferably surrounds each individual enclosure 51 .
  • the induced electromagnetic energy is transmitted at an effective frequency that allows the energy to substantially penetrate enclosure 51 wherein the induction energy transmits substantially throughout the volume of thermal transmitters 52 so that the temperature of the thermal transmitters 52 may be as uniform as possible.
  • thermal transmitters 52 absorb the induced electromagnetic energy, thermal transmitters 52 are heated to an effective temperature that is sufficient to heat the fluid.
  • the operating temperatures of the thermal transmitters 52 will depend entirely on the desired temperature of the outlet temperature of the fluid.
  • the heating properties of the thermal transmitters 52 are attributable to their specific electrical conductivity and resistivity characteristics.
  • Thermal transmitters 52 can be any suitable shape and size that will fit enclosure 51 . It is preferred that the thermal transmitters 52 be of a cork screw shape about one inch in diameter and about three inches in length. It is also preferred that the thermal transmitters will be placed into the heating system 50 in random order. Other shapes of thermal transmitters 52 that my be utilized in the heating system may include but are not limited to: (a) rasching rings; (b) Pall rings; (c) Berl saddles; and (d) Intalox saddles, which are all conventional shapes for tower packings.
  • thermal transmitters 52 may be of a structured packing design wherein the structured packing will be comprised of an ordered geometry rather than a random packing configuration.
  • This embodiment will also include a combination of structured and random packing configuration as it would be obvious to one skilled in the art to combine these two configurations.
  • the thermal transmitters 52 will have an electrical resistance higher than about 100 ⁇ ohm-cm at 1800° F. and a thermal conductivity higher than about 195 BTU-in/ft 2 -hr-° F. at 1800° F.
  • the melting point of thermal transmitters 52 is preferably higher than the operating temperature of inductively heated system 50 and most preferably about 50° F. higher than the operating temperature of inductively heated system 50 .
  • the preferred melting point of thermal transmitters 52 is higher than about 1000° F., the more preferred is higher than about 1500° F., and the most preferred is higher than about 2000° F.
  • thermal transmitters 52 The preferred material for thermal transmitters 52 is silicone carbide or a composite thereof. In addition, it is preferred that the material for thermal transmitters 52 be comprised of a substantially non-magnetizable material. It should be understood, however, that any other materials that meet the above referenced melting point, thermal conductivity, and electrical resistivity can be used for constructing thermal transmitters 52 . Thermal transmitters 52 may be of sufficient quantity and shape to disturb the flowing fluids sufficiently to knock out any entrained solid particles carried by the fluid stream thus acting as a particulate scrubber.
  • heating system 50 can be operated in parallel with at least one additional heating system.
  • heating system 50 can be operated with at least one additional heating system placed in series with heating system 50 .
  • a filter 55 is installed at about the outlet of the enclosure 5 1 .
  • This filter is purely optional and the heating system can be operated without the filter 55 .
  • This filter 55 is preferably made of materials which are compatible with or the same as thermal transmitters 52 wherein filter 55 will have an electrical resistance higher than about 100 ⁇ ohm-cm at 1800° F. and a thermal conductivity higher than about 195 BTU-in/ft 2 -hr-° F. at 1800° F.
  • the melting point of filter 55 is preferably higher than the operating temperature of inductively heated system 50 and most preferably about 50° F. higher than the operating temperature of induction heating system.
  • Filter 55 will also preferably be comprised of a honeycomb structure capable of screening out at least a portion of any particulates that may have passed through induction heating system. Filter 55 may also be comprised of any effective structure that is suitable for screening out such particulates.
  • thermal transmitters 52 could be coated or impregnated with a catalyst to help drive various chemical reactions, including but not limited to an endothermic steam reforming reaction.
  • a filter 55 in the heating system to capture any particulate.
  • the inductively heated filter 55 could provide enough heat to cause the particulate to further react and exit the system.
  • the filter would prevent particulates from entering a downstream process.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Inorganic Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Thermal Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electromagnetism (AREA)
  • Processing Of Solid Wastes (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • General Induction Heating (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
US11/713,142 2006-03-02 2007-03-02 Induction heater Abandoned US20070210075A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US11/713,142 US20070210075A1 (en) 2006-03-02 2007-03-02 Induction heater

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US77924706P 2006-03-02 2006-03-02
US11/713,142 US20070210075A1 (en) 2006-03-02 2007-03-02 Induction heater

Publications (1)

Publication Number Publication Date
US20070210075A1 true US20070210075A1 (en) 2007-09-13

Family

ID=38475392

Family Applications (2)

Application Number Title Priority Date Filing Date
US11/713,440 Active 2032-05-26 US8647401B2 (en) 2006-03-02 2007-03-02 Steam reformation system
US11/713,142 Abandoned US20070210075A1 (en) 2006-03-02 2007-03-02 Induction heater

Family Applications Before (1)

Application Number Title Priority Date Filing Date
US11/713,440 Active 2032-05-26 US8647401B2 (en) 2006-03-02 2007-03-02 Steam reformation system

Country Status (2)

Country Link
US (2) US8647401B2 (fr)
WO (2) WO2007103131A2 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012015685A1 (fr) * 2010-07-27 2012-02-02 Gilbarco Inc. Distributeur de combustible ou de fluide d'échappement diesel, doté d'un système de régulation et de conditionnement de température de fluide
US11219331B2 (en) * 2016-05-03 2022-01-11 Rheavendors Services S.P.A. Apparatus for preparing and dispensing beverages
US11555473B2 (en) 2018-05-29 2023-01-17 Kontak LLC Dual bladder fuel tank
US11638331B2 (en) 2018-05-29 2023-04-25 Kontak LLC Multi-frequency controllers for inductive heating and associated systems and methods

Families Citing this family (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7833512B2 (en) * 2007-01-16 2010-11-16 Peter Pulkrabek Production of synthesis gas from biomass and any organic matter by reactive contact with superheated steam
US20090151251A1 (en) * 2007-12-17 2009-06-18 Range Fuels, Inc. Methods and apparatus for producing syngas and alcohols
WO2009102297A1 (fr) * 2008-02-11 2009-08-20 Peter Pulkrabek Production de gaz de biosynthèse à partir de biomasse et/ou de toutes matières organiques par hydropyrolyse éclair
US20100018113A1 (en) * 2008-06-26 2010-01-28 Casella Waste Systems, Inc. Engineered fuel feed stock
CN109536234A (zh) 2008-06-26 2019-03-29 谐和能源有限责任公司 用于取代烧煤工厂中的煤的工程燃料原料
US8444721B2 (en) * 2008-06-26 2013-05-21 Re Community Energy, Llc Engineered fuel feed stock
US9406957B2 (en) * 2008-07-23 2016-08-02 Green Light Industries, Inc. Hydrogen extraction
DE202009008671U1 (de) * 2009-06-24 2009-10-08 Kuntschar, Walter Vergaser zur Erzeugung von Schwachgas
PL2516926T3 (pl) 2009-12-22 2017-11-30 Accordant Energy, Llc Przerobione surowce paliwowe zawierające sorbent
US8562699B2 (en) 2010-06-16 2013-10-22 C6 Technologies, Inc. Pyrolysis waste and biomass treatment
WO2012015812A2 (fr) * 2010-07-27 2012-02-02 Heritage Environmental Services, Llc Gazogène chauffé par induction
US20130067800A1 (en) * 2010-12-08 2013-03-21 Karim Wahdan Thermodepolymerization of plastic using induction heating
EP3450526A1 (fr) 2012-01-26 2019-03-06 Accordant Energy, LLC Atténuation d'émissions de combustion nocives à l'aide de sorbant contenant des charges de combustible modifiées
GB2499404B (en) * 2012-02-14 2019-08-14 Anergy Ltd Fuel processing using pyrolyser
US20140073823A1 (en) * 2012-09-10 2014-03-13 Phillips 66 Company Generating deoxygenated pyrolysis vapors
US20140069010A1 (en) * 2012-09-10 2014-03-13 Phillips 66 Company Generating deoxygenated pyrolysis vapors
US10144874B2 (en) 2013-03-15 2018-12-04 Terrapower, Llc Method and system for performing thermochemical conversion of a carbonaceous feedstock to a reaction product
US9376639B2 (en) 2013-03-15 2016-06-28 Terrapower, Llc Method and system for performing gasification of carbonaceous feedstock
CN103756727B (zh) * 2014-01-21 2016-01-20 刘平清 一种不产生碳排放的生产合成气的新方法
EP3099363A4 (fr) * 2014-01-31 2018-03-28 Cannakorp, Inc. Procédés et appareil de production de vapeur à base d'herbes
US10399086B2 (en) * 2015-02-09 2019-09-03 Viradys Medical Waste Solutions, LLC System and method for disinfecting medical waste
WO2017036794A1 (fr) 2015-08-28 2017-03-09 Haldor Topsøe A/S Chauffage par induction de réactions endothermiques
DE102015013071A1 (de) * 2015-10-08 2017-04-13 Linde Aktiengesellschaft Induktives Heizen eines Dampfreformerofens
WO2017072057A1 (fr) 2015-10-28 2017-05-04 Haldor Topsøe A/S Déshydrogénation d'alcanes
CA2970521A1 (fr) * 2016-06-13 2017-12-13 Hydra Heating Industries, LLC Transport de fluide au moyen de chauffage inductif
WO2018176026A1 (fr) 2017-03-24 2018-09-27 Terrapower, Llc Procédé et système de recyclage de gaz résiduaire de pyrolyse par conversion en acide formique
US10787610B2 (en) 2017-04-11 2020-09-29 Terrapower, Llc Flexible pyrolysis system and method
WO2020035574A1 (fr) * 2018-08-16 2020-02-20 Basf Se Dispositif et procédé de chauffage d'un fluide dans une conduite tubulaire
WO2020150247A1 (fr) * 2019-01-15 2020-07-23 Sabic Global Technologies, B.V. Utilisation d'énergie renouvelable dans la synthèse de méthanol
US11447576B2 (en) 2019-02-04 2022-09-20 Eastman Chemical Company Cellulose ester compositions derived from recycled plastic content syngas
US11370983B2 (en) 2019-02-04 2022-06-28 Eastman Chemical Company Gasification of plastics and solid fossil fuels
WO2020205404A1 (fr) 2019-03-29 2020-10-08 Eastman Chemical Company Polymères, articles et produits chimiques fabriqués à partir de gaz de synthèse dérivé de textiles densifiés
KR102272034B1 (ko) * 2019-11-07 2021-07-02 한국에너지기술연구원 고형 폐기물 연료(srf)의 열분해 가스화 및 알루미늄 재활용 장치
CN111667937A (zh) * 2020-04-30 2020-09-15 中国辐射防护研究院 一种用于处理放射性废物的蒸汽重整固定床反应器
JP7406801B2 (ja) 2020-05-07 2023-12-28 トクデン株式会社 過熱水蒸気生成装置
US20220252258A1 (en) * 2021-01-21 2022-08-11 Gary M. Gariglio Material conversion apparatus
WO2023172776A2 (fr) * 2022-03-11 2023-09-14 The Board Of Trustees Of The Leland Stanford Junior University Chauffage par induction avec suscepteurs de métamatériau pour systèmes de réacteur chimique

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2406640A (en) * 1944-01-05 1946-08-27 Gulf Oil Corp Conversion of hydrocarbons at high rates of heat input
US3445616A (en) * 1966-12-06 1969-05-20 Corning Glass Works Electric flame generator
US3671715A (en) * 1970-06-01 1972-06-20 Henry J Burnett Electric induction gas heater
US3826895A (en) * 1972-05-10 1974-07-30 Schladitz Whiskers Ag Electrical fluid heating device
US3934117A (en) * 1973-03-27 1976-01-20 Schladitz Hermann J Electric fluid heating device
US4331854A (en) * 1980-02-28 1982-05-25 Maryland Cup Corporation Low frequency induction heater
US4341936A (en) * 1979-12-17 1982-07-27 Virgin George C Electromagnetic induction energy converter
US5319170A (en) * 1992-10-20 1994-06-07 Belmont Instrument Corporation Induction fluid heater utilizing a shorted turn linking parallel flow paths
US5324904A (en) * 1988-10-03 1994-06-28 Imperial Chemical Industries Plc Reactors for effecting chemical processes
US6175689B1 (en) * 1999-06-10 2001-01-16 Byron Blanco, Jr. In-line tankless electrical resistance water heater
US6240250B1 (en) * 1999-06-10 2001-05-29 Byron Blanco, Jr. Compact in-line tankless double element water heater
US6504136B2 (en) * 2000-02-19 2003-01-07 Malcolm Robert Snowball Liquid heating apparatus with an inductively heated impeller
US6574426B1 (en) * 2002-11-18 2003-06-03 Byron Blanco, Jr. In-line tankless instantaneous electrical resistance water heater
US6967315B2 (en) * 2002-06-12 2005-11-22 Steris Inc. Method for vaporizing a fluid using an electromagnetically responsive heating apparatus

Family Cites Families (40)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3714911A (en) * 1971-03-10 1973-02-06 Sterling Drug Inc Method of treatment of alkaline pulping black liquors by wet air oxidation
US4437417A (en) * 1982-11-15 1984-03-20 Texaco Inc. Environmentally safe process for disposing of toxic inorganic CN-containing sludge
US4602140A (en) * 1984-11-01 1986-07-22 Mangels Industrial S.A. Induction fluid heater
US4874587A (en) * 1986-09-03 1989-10-17 Thermolytic Decomposer Hazardous waste reactor system
GB8722847D0 (en) 1987-09-29 1987-11-04 Electricity Council Performing endothermic catalytic reactions
FR2653044B1 (fr) * 1989-10-12 1992-03-27 Pec Engineering Procede et dispositifs de decontamination de produits solides.
US5319176A (en) * 1991-01-24 1994-06-07 Ritchie G. Studer Plasma arc decomposition of hazardous wastes into vitrified solids and non-hazardous gasses
US5134944A (en) * 1991-02-28 1992-08-04 Keller Leonard J Processes and means for waste resources utilization
US5286942A (en) * 1991-10-24 1994-02-15 Arthur D. Little Enterprises, Inc. Induction steam humidifier
DE59205475D1 (de) * 1991-11-29 1996-04-04 Noell En Und Entsorgungstechni Verfahren zur thermischen Verwertung von Abfallstoffen
FR2685760B3 (fr) * 1991-12-30 1993-11-26 Ind Tech Res Inst Appareil a eau chaude instantanee.
FR2686347B1 (fr) * 1992-01-22 1994-10-07 Lorraine Carbone Procede de pyrolyse d'effluents fluides et dispositif correspondant.
US5273556A (en) * 1992-03-30 1993-12-28 Texaco Inc. Process for disposing of sewage sludge
US5254318A (en) * 1992-07-20 1993-10-19 Stone & Webster Engineering Corporation Lined reformer tubes for high pressure reformer reactors
US5821111A (en) * 1994-03-31 1998-10-13 Bioengineering Resources, Inc. Bioconversion of waste biomass to useful products
US5334819A (en) * 1993-11-08 1994-08-02 Lin Hsiao Chih Instant heating type water heaters
US5958273A (en) * 1994-02-01 1999-09-28 E. I. Du Pont De Nemours And Company Induction heated reactor apparatus
US5922090A (en) * 1994-03-10 1999-07-13 Ebara Corporation Method and apparatus for treating wastes by gasification
US5602297A (en) * 1995-02-08 1997-02-11 Wang; Chi-Shang Multistage double closed-loop process for waste decontamination
US6398921B1 (en) * 1995-03-15 2002-06-04 Microgas Corporation Process and system for wastewater solids gasification and vitrification
US6084147A (en) * 1995-03-17 2000-07-04 Studsvik, Inc. Pyrolytic decomposition of organic wastes
JPH08264272A (ja) * 1995-03-27 1996-10-11 Seta Giken:Kk 電磁誘導加熱装置
US5710360A (en) * 1995-03-31 1998-01-20 Vanish, Inc. Thermal desorption system for decontaminating materials
DE19512785A1 (de) * 1995-04-05 1996-10-17 Siemens Ag Verfahren zur thermischen Behandlung von Abfallstoffen
WO1997034445A1 (fr) * 1996-03-15 1997-09-18 Bbmr Limited Appareil de chauffage de fluides par induction
US6112675A (en) * 1996-04-08 2000-09-05 Foster Wheeler Environmental Corporation Process and apparatus for treating process streams from a system for separating constituents from contaminated material
US5980858A (en) * 1996-04-23 1999-11-09 Ebara Corporation Method for treating wastes by gasification
US6902711B1 (en) * 1996-04-23 2005-06-07 Ebara Corporation Apparatus for treating wastes by gasification
US5878752A (en) * 1996-11-25 1999-03-09 Philip Morris Incorporated Method and apparatus for using, cleaning, and maintaining electrical heat sources and lighters useful in smoking systems and other apparatuses
US5879566A (en) * 1997-02-03 1999-03-09 The Scientific Ecology Group, Inc. Integrated steam reforming operation for processing organic contaminated sludges and system
US6187465B1 (en) * 1997-11-07 2001-02-13 Terry R. Galloway Process and system for converting carbonaceous feedstocks into energy without greenhouse gas emissions
SG68092A1 (en) * 1998-02-20 1999-10-19 Meidensha Electric Mfg Co Ltd Process and system for treating material containing noxious components
TWI241392B (en) * 1999-09-20 2005-10-11 Japan Science & Tech Agency Apparatus and method for gasifying solid or liquid fuel
US6497856B1 (en) * 2000-08-21 2002-12-24 H2Gen Innovations, Inc. System for hydrogen generation through steam reforming of hydrocarbons and integrated chemical reactor for hydrogen production from hydrocarbons
US6619218B2 (en) * 2000-12-05 2003-09-16 San Iku Co., Ltd. Method and apparatus for making a pollutant harmless
US6709602B2 (en) * 2001-04-23 2004-03-23 General Atomics Process for hydrothermal treatment of materials
US7070743B2 (en) * 2002-03-14 2006-07-04 Invista North America S.A R.L. Induction-heated reactors for gas phase catalyzed reactions
WO2005022038A2 (fr) * 2003-08-21 2005-03-10 International Environmental Solutions Corporation Support de chambre pour systeme de traitement pyrolytique de dechets
US7022953B2 (en) * 2004-06-03 2006-04-04 Fyne Industries, L.L.C. Electromagnetic flowing fluid heater
MX2007008729A (es) * 2005-01-18 2008-03-04 Enquest Power Corp Metodo para reformado por vapor de material carbonaceo.

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2406640A (en) * 1944-01-05 1946-08-27 Gulf Oil Corp Conversion of hydrocarbons at high rates of heat input
US3445616A (en) * 1966-12-06 1969-05-20 Corning Glass Works Electric flame generator
US3671715A (en) * 1970-06-01 1972-06-20 Henry J Burnett Electric induction gas heater
US3826895A (en) * 1972-05-10 1974-07-30 Schladitz Whiskers Ag Electrical fluid heating device
US3934117A (en) * 1973-03-27 1976-01-20 Schladitz Hermann J Electric fluid heating device
US4341936A (en) * 1979-12-17 1982-07-27 Virgin George C Electromagnetic induction energy converter
US4331854A (en) * 1980-02-28 1982-05-25 Maryland Cup Corporation Low frequency induction heater
US5324904A (en) * 1988-10-03 1994-06-28 Imperial Chemical Industries Plc Reactors for effecting chemical processes
US5319170A (en) * 1992-10-20 1994-06-07 Belmont Instrument Corporation Induction fluid heater utilizing a shorted turn linking parallel flow paths
US6175689B1 (en) * 1999-06-10 2001-01-16 Byron Blanco, Jr. In-line tankless electrical resistance water heater
US6240250B1 (en) * 1999-06-10 2001-05-29 Byron Blanco, Jr. Compact in-line tankless double element water heater
US6504136B2 (en) * 2000-02-19 2003-01-07 Malcolm Robert Snowball Liquid heating apparatus with an inductively heated impeller
US6967315B2 (en) * 2002-06-12 2005-11-22 Steris Inc. Method for vaporizing a fluid using an electromagnetically responsive heating apparatus
US6574426B1 (en) * 2002-11-18 2003-06-03 Byron Blanco, Jr. In-line tankless instantaneous electrical resistance water heater

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012015685A1 (fr) * 2010-07-27 2012-02-02 Gilbarco Inc. Distributeur de combustible ou de fluide d'échappement diesel, doté d'un système de régulation et de conditionnement de température de fluide
US20120024892A1 (en) * 2010-07-27 2012-02-02 Jack Francis Bartlett Fuel or def dispenser having fluid temperature conditioning and control system
CN103118970A (zh) * 2010-07-27 2013-05-22 吉尔巴科公司 具有流体温度调节和控制系统的燃料或def分配器
US8733590B2 (en) * 2010-07-27 2014-05-27 Gilbarco, Inc. Fuel or DEF dispenser having fluid temperature conditioning and control system
CN105084284A (zh) * 2010-07-27 2015-11-25 吉尔巴科公司 具有流体温度调节和控制系统的燃料或def分配器
CN105399036A (zh) * 2010-07-27 2016-03-16 吉尔巴科公司 具有流体温度调节和控制系统的燃料或def分配器
US9422147B2 (en) 2010-07-27 2016-08-23 Gilbarco Inc. Fuel or DEF dispenser having fluid temperature conditioning and control system
US11219331B2 (en) * 2016-05-03 2022-01-11 Rheavendors Services S.P.A. Apparatus for preparing and dispensing beverages
US11555473B2 (en) 2018-05-29 2023-01-17 Kontak LLC Dual bladder fuel tank
US11638331B2 (en) 2018-05-29 2023-04-25 Kontak LLC Multi-frequency controllers for inductive heating and associated systems and methods

Also Published As

Publication number Publication date
WO2007103283A2 (fr) 2007-09-13
US20070204512A1 (en) 2007-09-06
WO2007103283A3 (fr) 2007-12-13
US8647401B2 (en) 2014-02-11
WO2007103131A2 (fr) 2007-09-13
WO2007103131A3 (fr) 2008-07-17

Similar Documents

Publication Publication Date Title
US20070210075A1 (en) Induction heater
Lu et al. High temperature energy storage performances of methane reforming with carbon dioxide in a tubular packed reactor
US9115913B1 (en) Fluid heater
Adhikari et al. Kinetics and reactor modeling of hydrogen production from glycerol via steam reforming process over Ni/CeO2 catalysts
Balakotaiah et al. Modular reactors with electrical resistance heating for hydrocarbon cracking and other endothermic reactions
JPH06509419A (ja) 特に原子力設備におけるｈ↓２・空気・蒸気・混合物に含まれる水素の再結合および／又は点火方法と装置
Hong et al. Numerical study of effect of operating and design parameters for design of steam reforming reactor
WO2021195566A1 (fr) Production d'hydrogène et séquestration de carbone par craquage d'hydrocarbures dans un lit chauffé et fluidisé
Yuan et al. Heat transfer and energy storage performance of steam methane reforming in a tubular reactor
CN104946281A (zh) 一种生物质气化热解过程中强化焦油裂解的装置与方法
JP4399582B2 (ja) ガス加熱装置
Chen et al. Feasibility of using ammonia-based thermochemical energy storage to produce high-temperature steam or sCO2
Iwaniszyn et al. Experimental and CFD investigation of heat transfer and flow resistance in woven wire gauzes
Ho et al. Analytical and experimental studies of wire mesh packed double-pass solar air heaters under recycling operation
JP2000065312A (ja) 高温水蒸気発生装置、高温水蒸気を用いた処理装置及び有機系塩素含有物の脱塩素方法
Raymundo et al. Continuous fast pyrolysis of rice husk in a fluidized bed reactor with high feed rates
Chokphoemphun et al. Heat transfer of a coil-tube heat exchanger in the freeboard zone of a rice husk fluidized-bed combustor
Viereck et al. Assessment of heat exchangers for the integration of concentrated solar energy into the catalytic hydrothermal gasification of biomass
RU2193918C2 (ru) Способ индукционного поджига химической реакции
Čatipović et al. Experimental validation of the Adams‐Welty model for heat transfer in large‐particle fluidized beds
Stefanidis et al. Modeling ignition in catalytic microreactors
Yek et al. A novel microwave air heater integrated with thermal energy storage
Yoon et al. Numerical and experimental analysis of thermal-flow characteristics in a pyrolysis reactor of a gas scrubber designed based on similitude theory
SE423896B (sv) Kompakt katalytisk reaktionsapparaur for framstellning av gasprodukter ur kolvetebrenslen
Gutiérrez Ortiz et al. Heat Transfer Limitations in Supercritical Water Gasification

Legal Events

Date Code Title Description
AS Assignment

Owner name: SHAW WASTE SOLUTIONS, LLC, LOUISIANA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:COCHRAN, STEVE;SELF, JOHN;OLEXY, ROBERT A.;REEL/FRAME:019262/0743;SIGNING DATES FROM 20070326 TO 20070502

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION

AS Assignment

Owner name: SHAW INTELLECTUAL PROPERTY HOLDINGS, INC., LOUISIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SWS HOLDINGS, LLC;REEL/FRAME:024699/0009

Effective date: 20100426

Owner name: SWS HOLDINGS, LLC, LOUISIANA

Free format text: CHANGE OF NAME;ASSIGNOR:SHAW WASTE SOLUTIONS, LLC;REEL/FRAME:024699/0236

Effective date: 20090109