СПОСОБ ПИРОЛИЗА ОРГАНОСОДЕРЖАЩЕГО СЫРЬЯ

1. Способ пиролиза органосодержащего сырья путем термической обработки, включающий подготовку и подачу сырья в реактор через шлюзовую камеру загрузки, в которой его предварительно подвергают вакуумированию и отделяют от области термической обработки и окружающей среды, последующее осуществление пиролиза перерабатываемого сырья путем косвенного нагрева при температуре 450-500°C подаваемым в реактор теплоносителем с отделением образующейся твердой фазы, разделением жидкой и парогазообразной фаз, содержащих углерод и углеводороды, и эвакуацию твердых субстанций пиролиза через шлюзовую камеру выгрузки, размещенную в нижней части реактора, отличающийся тем, что для пиролиза используют, по меньшей мере, один реактор, который выполняют со сдвоенными стенками, в пространство между которыми осуществляют в процессе пиролиза непрерывную подачу предварительно разогретого теплоносителя, при этом теплоноситель подогревают посредством разогревающего котла, размещенного изолированно относительно реактора. ! 2. Способ по п.1, отличающийся тем, что перерабатываемое органосодержащее сырье перед подачей в реактор предварительно подвергают дроблению. ! 3. Способ по п.1, отличающийся тем, что перерабатываемое органосодержащее сырье подают в реактор в виде цельного продукта. ! 4. Способ по п.1, отличающийся тем, что в пространство между стенками реактора подают высокотемпературные органические теплоносители. ! 5. Способ по п.1, отличающийся тем, что в пространство между стенками реактора подают высокотемпературный теплоноситель в виде эвтектического сплава. ! 6. Способ по п.1, отличающийся тем, что рабочую зону реактора подог

Methods of recovering hydrocarbons from hydrocarbonaceous material using a constructed infrastructure and associated systems maintained under positivepressure.

Methods of recovering hydrocarbons from hydrocarbonaceous material using a constructed infrastructure and associated systems maintained under positivepressure.

Intermediate vapor collection within encapsulated control infrastructures.

Carbon management and sequestration from encapsulated control infrastructures.

Convective heat systems for recovery of hydrocarbons from encapsulated permeability control infrastructures.

Carbon management and sequestration from encapsulated control infrastructures.

Intermediate vapor collection within encapsulated control infrastructures.

Carbon management and sequestration from encapsulated control infrastructures.

Convective heat systems for recovery of hydrocarbons from encapsulated permeability control infrastructures.

METHODS OF RECOVERING HYDROCARBONS FROM HYDROCARBONACEOUS MATERIAL USING A CONSTRUCTED INFRASTRUCTURE AND ASSOCIATED SYSTEMS

A method of recovering hydrocarbons from hydro carbonaceous materials can include forming a constructed permeability control infrastructure (100). This constructed infrastructure defines a substantially encapsulated volume. A comminuted hydro carbonaceous material can be introduced into the control infrastructure to form a permeable body (120) of hydro carbonaceous material. The permeable body (120) can be heated sufficient to remove hydrocarbons therefrom such as by using heating conduits (118,126). During heating the hydro carbonaceous material is substantially stationary as the constructed infrastructure (100) is a fixed structure. Removed hydrocarbons can be collected as liquid products (136) and gaseous products (140) for further processing, use in the process, and/or use as recovered.

HYDROCARBON CONVERSION PROCESS

The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.

Oven drying and roasting

ИНФРАСТРУКТУРА С КОНТРОЛИРОВАННОЙ ПРОНИЦАЕМОСТЬЮ И СПОСОБ ПОЛУЧЕНИЯ УГЛЕВОДОРОДОВ ИЗ УГЛЕВОДОРОДСОДЕРЖАЩИХ МАТЕРИАЛОВ

Заявлена сооруженная инфраструктура с контролируемой проницаемостью, которая включает: а) накопительный резервуар с контролируемой проницаемостью, который определяет, по сути, замкнутый объем, b) раздробленный углеводородсодержащий материал внутри замкнутого объема, формируя проницаемый массив из углеводородсодержащего материала, и с) по крайней мере, один возбуждающий конвекцию трубопровод, размещенный в нижней части проницаемого массива, для генерирования объемных схем конвективных потоков через проницаемый массив и способ получения углеводородов из углеводородсодержащих материалов, который включает стадии, в которых: а) формируют сооруженную инфраструктуру с контролируемой проницаемостью, которая определяет, по сути, замкнутый объем, b) вводят раздробленный углеродсодержащий материал в контролируемую инфраструктуру с образованием проницаемого массива из углеродсодержащего материала, с) пропускают нагретую текущую среду по объемным схемам конвективных потоков через проницаемый массив, ...

INSTALLATION OF THERMAL DECOMPOSITION OF AND HIGH TEMPERATURE FURNACE

КОНТРОЛЬ И СВЯЗЫВАНИЕ УГЛЕРОДА ИЗ ГЕРМЕТИЗИРОВАННЫХ КОНТРОЛИРУЕМЫХ ИНФРАСТРУКТУР

Способ связывания выбросов диоксида углерода во время извлечения углеводородов из углеводородсодержащих материалов может включать стадию, в которой формируют сооруженную инфраструктуру (100) с контролируемой проницаемостью. Эта сооруженная инфраструктура (100) определяет, по существу, замкнутый объем. Раздробленный углеводородсодержащий материал может быть введен в контролируемую инфраструктуру (100) с образованием проницаемого массива (120) из углеводородсодержащего материала. Проницаемый массив (120) может быть нагрет в достаточной степени для удаления из него углеводородов. Во время нагревания углеводородсодержащий материал является, по существу, неподвижным, так как сооруженная инфраструктура (100) представляет собой фиксированную конструкцию. Дополнительно во время нагревания может быть связан любой диоксид углерода, который образуется. Удаленные углеводороды могут быть собраны для дальнейшей обработки, использованы в процессе и/или применены в том виде, как получены.

КОНТРОЛЬ И СВЯЗЫВАНИЕ УГЛЕРОДА ИЗ ГЕРМЕТИЗИРОВАННЫХ КОНТРОЛИРОВАННЫХ ИНФРАСТРУКТУР

Заявлен способ связывания выбросов диоксида углерода во время добывания углеводородов из углеводородсодержащих материалов, который включает стадии, в которых: а) формируют сооруженную инфраструктуру с контролированной проницаемостью, которая определяет, по сути, замкнутый объем, b) вводят раздробленный углеводородсодержащий материал в контролированную инфраструктуру с образованием проницаемого массива из углеводородсодержащего материала, с) нагревают проницаемый массив достаточной мерой для удаления из него углеводородов так, что углеводородсодержащий материал является, по сути, неподвижным во время нагревания и d) связывают диоксид углерода, выделяемый из проницаемого массива во время нагревания, и е) собирают удаленные углеводороды и сооруженную инфраструктуру с контролированной проницаемостью, которая включает: а) накопительный резервуар с контролированной проницаемостью, который определяет, по сути, замкнутый объем, причем накопительный резервуар с контролированной проницаемостью, по ...

СПОСОБЫ ИЗВЛЕЧЕНИЯ УГЛЕВОДОРОДОВ ИЗ УГЛЕВОДОРОДСОДЕРЖАЩЕГО МАТЕРИАЛА С ИСПОЛЬЗОВАНИЕМ СООРУЖЕННОЙ ИНФРАСТРУКТУРЫ И СВЯЗАННЫХ С НЕЙ СИСТЕМ, КОТОРЫЕ ПОДДЕРЖИВАЮТСЯ ПРИ ИЗБЫТОЧНОМ ДАВЛЕНИИ

Изобретение относится к способу добывания углеводородов из углеводородсодержащего материала. Заявлен способ извлечения углеводородов из углеводородсодержащих материалов, который включает стадии, на которых: а) формируют сооруженную инфраструктуру с контролированной проницаемостью, которая образует, по сути, замкнутый объем, b) вводят раздробленный углеродсодержащий материал в контролированную инфраструктуру для образования проницаемого массива из углеводородсодержащего материала, с) поддерживают внутри указанного замкнутого объема избыточное давление относительно давления снаружи указанной контролированной инфраструктуры, причем избыточное давление является достаточным, чтобы, по сути, предупредить поступление кислорода или других газообразных окислителей снаружи указанной контролированной инфраструктуры в указанный замкнутый объем, d) пропускают газообразную текущую среду, что, по сути, не содержит кислорода, через проницаемый массив, чтобы, по сути, удалить углеводороды и другие газообразные ...

ПРОМЕЖУТОЧНЫЙ СБОР ПАРОВ ВНУТРИ ГЕРМЕТИЗИРОВАННЫХ КОНТРОЛИРУЕМЫХ ИНФРАСТРУКТУР

Способ извлечения углеводородов из углеводородсодержащих материалов может включать формирование сооруженной инфраструктуры (600) с контролируемой проницаемостью. Эта сооруженная инфраструктура (600) определяет, по существу, замкнутый объем. Добытый углеводородсодержащий материал может быть введен в контролируемую инфраструктуру с образованием проницаемого массива (605) из углеводородсодержащего материала. Проницаемый массив (605) может быть нагрет в достаточной степени для удаления из него углеводородов. Углеводородные продукты могут быть собраны из промежуточных местоположений (620, 630) внутри проницаемого массива (605). Система (610) промежуточного сбора текучих сред может быть преимущественно использована для выведения углеводородного продукта из проницаемого массива (605) в предварительно выбранных местоположениях. Такой промежуточный сбор может давать фракции углеводородного продукта, которые могут сокращать или устранять необходимость в полномасштабной дистилляции углеводородного ...

СПОСОБЫ ИЗВЛЕЧЕНИЯ УГЛЕВОДОРОДОВ ИЗ УГЛЕВОДОРОДСОДЕРЖАЩЕГО МАТЕРИАЛА С ИСПОЛЬЗОВАНИЕМ СООРУЖЕННОЙ ИНФРАСТРУКТУРЫ И СВЯЗАННЫХ С НЕЮ СИСТЕМ, ПОДДЕРЖИВАЕМЫХ ПРИ ИЗБЫТОЧНОМ ДАВЛЕНИИ

Способ извлечения углеводородов из углеводородсодержащих материалов может включать стадию, в которой формируют сооруженную инфраструктуру (100) с контролируемой проницаемостью. Эта сооруженная инфраструктура (100) образует, по существу, замкнутый объем. Раздробленный углеводородсодержащий материал может быть введен в контролируемую инфраструктуру с образованием проницаемого массива (120) из углеводородсодержащего материала. Проницаемый массив (120) может быть нагрет в достаточной степени для удаления из него углеводородов. Во время нагревания и удаления углеводородов и после этого внутри замкнутого объема может поддерживаться избыточное давление с помощью неокислительного газа, чтобы способствовать промыванию углеводородсодержащего материала, подавлению нежелательного поступления кислорода в замкнутый объем и удалению извлекаемых углеводородов после процесса нагревания.

CONVECTIVE HEAT SYSTEMS FOR RECOVERY OF HYDROCARBONS FROM ENCAPSULATED PERMEABILITY CONTROL INFRASTRUCTURES

Gasifier for biomass comprising organic effluents and wastes, burns pyrolysis gas for indirect heating of separate chamber containing wastes

Intense combustion of a fuel gas (4) takes place in a first chamber with flue duct (5). Heat is transferred by conduction through the sealed wall (6) into the second chamber (2). The feeder (19) supplies organic material high in this chamber; a char (9) extractor operates at the base. Pyrolysis and slow combustion take place in the second chamber. The low gas offtake (10) extracts combustible gas. Some or all of this is passed through the duct (11) to the fuel gas burner inlet (4) of the first chamber. An Independent claim is included for the corresponding pyrolysis reactor. Preferred features: The second chamber is in thermal contact through a sealed wall (12) with a third chamber (3), i.e. a heat exchange jacket, through which water or steam flows. Gas produced in the second chamber passes down through it, to be extracted at the base. The char is collected in a container (16) to which the flue from the first chamber is connected. The flue gases are purified by passing them through the active carbon constituting the char.

gestao e sequestro de carbono a partir de infraestuturas de controle encapsuladas

Wasted electronic product processing method and processing apparatus thereof capable of greatly improving the practicality of the wasted electronic products

The present invention provides a wasted electronic product processing method and a processing apparatus thereof. The method includes conveying a plurality of wasted electronic products under processing to a vacuum cracking device; subjecting the plastic materials in the wasted electronic products to a low-temperature vacuum cracking for generating gaseous oil and gas so as to avoid generation of toxic gas and gas explosion phenomenon, which is cost-saving, safe and eco-friendly in use; heating and melting the metal material into liquid metal by a high-temperature vacuum cracking; and using a filtering device, an electrolysis device and a separation device to separately process the gaseous oil and gas and the liquid metal so as to obtain liquid oil, liquid hydrogen chloride, gaseous auxiliary fuel, and solid metal, thereby greatly improving the practicality of the wasted electronic products and thus providing a wasted electronic product processing method and a processing apparatus thereof ...

Утилизация высвобождаемых средств индивидуальной защиты способом бескислородного термического пиролиза

FIELD: waste processing and disposal.SUBSTANCE: invention relates to disposal of released military creature, namely to method of recycling rubber wastes of personal protective equipment (PPE) by means of oxygen free thermal pyrolysis, which consists in decomposition of initial fragments of PPE to end pyrolysis products, suitable for further use in various industries.EFFECT: method considerably reduces atmospheric pollution compared to the process of simple combustion, and the substances obtained as a result of pyrolysis, which are similar to products of oil cracking, represent material for petrochemical synthesis.1 cl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 712 616 C1 (51) МПК C10B 47/02 (2006.01) B09B 3/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C10B 47/02 (2019.08); B09B 3/00 (2019.08) (21)(22) Заявка: 2019100455, 09.01.2019 (24) Дата начала отсчета срока действия патента: Дата регистрации: 29.01.2020 (45) Опубликовано: 29.01.2020 Бюл. № 4 2 7 1 2 6 1 6 R U (56) Список документов, цитированных в отчете о поиске: RU 2212430 С1, 20.09.2003. RU 2089786 C1, 10.09.1997. UА 15645 U, 17.07.2006. US 6833485 B2, 21.12.2004. WO 2014032843 A1, 06.03.2014. US 4284616 A, 18.08.1981. Mahmood M.Barbooti, et al., ''Optimization of pyrolysis conditions of scrap tires under inert gas atmosphere'', JOURNAL of ANALYTICAL and APPLIED PYROLYSIS, 72, 2004, PP.165-170, (см. прод.) (54) Утилизация высвобождаемых средств индивидуальной защиты способом бескислородного термического пиролиза (57) Реферат: Изобретение относится к утилизации использованию в различных областях высвобождаемого военного существа, а именно промышленности. Способ существенно снижает к способу утилизации резиновых отходов средств загрязнения атмосферы по сравнению с индивидуальной зашиты (СИЗ) путем процессом простого сжигания, а полученные в бескислородного термического пиролиза, результате пиролиза вещества, сходные с заключающегося в разложении ...

УСТРОЙСТВО И СПОСОБ ПИРОЛИЗА УГЛЯ С ШИРОКИМ ДИАПАЗОНОМ РАЗМЕРОВ ЧАСТИЦ

FIELD: chemistry. SUBSTANCE: coal is fed into a pyrolysis apparatus through an inlet 5 and placed at both sides of a pyrolysis gas channel 2. The coal is heated in the pyrolysis apparatus. Gaseous pyrolysis products are collected in a pyrolysis gas channel 2 through an opening on the surface of its wall and output through a pipe 4. The solid product is unloaded through a semicoke outlet 1. EFFECT: invention increases mass and heat exchange during coal pyrolysis. 10 cl, 6 dwg, 2 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (51) МПК C10B 53/04 (13) 2 576 437 C1 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2014140938/05, 16.03.2012 (24) Дата начала отсчета срока действия патента: 16.03.2012 (45) Опубликовано: 10.03.2016 Бюл. № 7 (73) Патентообладатель(и): ИНСТИТЬЮТ ОФ ПРОЦЕСС ИНДЖИНИРИНГ, ЧАЙНИЗ АКАДЕМИ ОФ САЙНСИС (CN) (85) Дата начала рассмотрения заявки PCT на национальной фазе: 16.10.2014 (86) Заявка PCT: CN 2012/000331 (16.03.2012) 2 5 7 6 4 3 7 (56) Список документов, цитированных в отчете о поиске: CN 102212378 A, 12.10.2011. RU 2437914 C2, 27.12.2011. US 3736233 A, 29.05.1973. CN 101818071 A, 01.09.2010. CN 101984023 A, 09.03.2011. R U Приоритет(ы): (22) Дата подачи заявки: 16.03.2012 (72) Автор(ы): Сюй Гуанвэнь (CN), Хань Цзянцзэ (CN), У Жунчэн (CN), Чжан Чунь (CN), Гао Шицю (CN), Чжан Цзюйвэй (CN) (87) Публикация заявки PCT: 2 5 7 6 4 3 7 R U Адрес для переписки: 634050, г.Томск, а/я 86, ООО "АИС-БП", директору, патентному поверенному РФ (рег.N 193) Л.В.Бутенко (54) УСТРОЙСТВО И СПОСОБ ПИРОЛИЗА УГЛЯ С ШИРОКИМ ДИАПАЗОНОМ РАЗМЕРОВ ЧАСТИЦ (57) Реферат: Изобретение относится к области угольнохимической промышленности. Уголь загружают в устройство для пиролиза через вход 5 и размещают его по обеим сторонам канала 2 газа пиролиза. Уголь нагревают в устройстве пиролиза. Собирают газообразные продукты пиролиза в канал 2 газа пиролиза через отверстия на поверхности его стенки и выводят их через трубу 4. ...

Datenausgabepuffer und Halbleiterspeicherbauelement

Datenausgabepuffer, der einer Pufferausgabeleitung (EDIO) Daten, die von einer Puffereingabeleitung (IDIO) empfangen werden, wahlweise in einem normalen Ausgabemodus oder einem erweiterten Datenausgabemodus zur Verfügung stellt und dazu folgende Elemente enthält: eine Verzögerungssteuereinheit (100), die dafür eingerichtet ist, in Reaktion auf ein empfangenes periodisches Referenzsteuersignal (RCON) ein Pufferfreigabesignal (BEN) zu erzeugen, das periodisch abwechselnd einen aktivierten und einen deaktivierten Zustand in Zeiträumen einnimmt, in denen eine Periodendauer des Referenzsteuersignals (RCON) länger als eine Referenzperiodendauer ist, um den normalen Ausgabemodus auszuwählen, und das kontinuierlich im aktivierten Zustand in Zeiträumen gehalten wird, in denen die Periodendauer des Referenzsteuersignals (RCON) kürzer als die Referenzperiodendauer ist, um den erweiterten Datenausgabemodus auszuwählen, und eine Puffereinheit (200), die dafür eingerichtet ist, der Pufferausgabeleitung ...

Carbon management and sequestration from encapsulated control infrastructures

A method of sequestering carbon dioxide emissions during recovery of hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (100). This constructed infrastructure (100) defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure (100) to form a permeable body (120) of hydrocarbonaceous material. The permeable body (120) can be heated sufficient to remove hydrocarbons therefrom. During heating, the hydrocarbonaceous material is substantially stationary as the constructed infrastructure (100) is a fixed structure. Additionally, during heating, any carbon dioxide that is produced can be sequestered. Removed hydrocarbons can be collected for further processing, use in the process, and/or use as recovered.

Methods of recovering hydrocarbons from hydrocarbonaceous material using a constructed infrastructure and associated systems maintained under positive pressure

A method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (100). This constructed infrastructure (100) defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body (120) of hydrocarbonaceous material. The permeable body (120) can be heated sufficient to remove hydrocarbons therefrom. During heating and removal of hydrocarbons and subsequent thereto a positive pressure can be maintained within the encapsulated volume by means of a non-oxidizing gas to expedite flushing of hydrocarbonaceous material, inhibit unwanted entry of oxygen into the encapsulated volume and remove recoverable hydrocarbons following the heating process.

PROCESS FOR VACUUM PYROLYSIS REMOVAL OF POLYMERS FROM VARIOUS OBJECTS

ABSTRACT OF THE DISCLOSURE Process for pyrolysis of polymeric organic compounds to remove or retrieve them from objects or materials that are substantially unaffected by the applied heat. The steps include heating in a first vacuum chamber to render flowable such polymers as are fusible at a temperature below that at which appreciable degrad-ation is initiated. The fused polymer drops by free fall from the first chamber to a second vacuum chamber in space communicating relation therewith but maintained at a substantially lower temp-erature, where the polymer resolidifies. Upon further heating, polymer remaining in the first chamber is volatilized and withdrawn from the chamber to a water mist scrubber where it is largely trapped. Remaining vapors in the scrubber are drawn through a vapor separator to a vent stack. After the combustible volatiles are removed from the first chamber, air is admitted into the chamber to oxidize any residual carbon ash, leaving only the inorganic residue which is easily removable from the objects or materials that were not affected by the pyrolysis action.

METHOD OF HIGH TEMPERATURE OF THE THERMAL DECOMPOSITION IN THE PROCESSING OF OIL-BEARING SHALE

СИСТЕМЫ КОНВЕКТИВНОГО НАГРЕВАНИЯ ДЛЯ ИЗВЛЕЧЕНИЯ УГЛЕВОДОРОДОВ ИЗ ГЕРМЕТИЗИРОВАННЫХ ИНФРАСТРУКТУР С КОНТРОЛИРУЕМОЙ ПРОНИЦАЕМОСТЬЮ

Сооруженная инфраструктура (100) с контролируемой проницаемостью может включать накопительный резервуар с контролируемой проницаемостью, который определяет, по существу, замкнутый объем. Инфраструктура (100) также может включать раздробленный углеводородсодержащий материал внутри замкнутого объема. Раздробленный углеводородсодержащий материал может формировать проницаемый массив (120) из углеводородсодержащего материала. Инфраструктура (100) может дополнительно включать по меньшей мере один возбуждающий конвекцию трубопровод, размещенный в нижней части проницаемого массива (120), для генерирования объемных схем конвективных потоков через проницаемый массив (120). Связанный с этим способ получения углеводородов из углеводородсодержащих материалов может включать стадию, в которой формируют сооруженную инфраструктуру (100) с контролируемой проницаемостью, которая определяет, по существу, замкнутый объем. Раздробленный углеводородсодержащий материал может быть введен в контролируемую инфраструктуру ...

USE OF SPENT CLAY SHALE OR ASH, OBTAINED BY METHODS OF DECOMPOSITION OF OIL-BEARING SHALE, WITH ADDITIVES OR WITHOUT THEM IN THE FORM OF SOLID FUEL

СПОСОБ ПИРОЛИЗА ОРГАНОСОДЕРЖАЩЕГО СЫРЬЯ

Изобретение относится к области переработки органосодержащего сырья. Способ пиролиза органосодержащего сырья включает подготовку и подачу сырья в реактор через шлюзовую камеру загрузки, в которой его предварительно подвергают вакуумированию и отделяют от области термической обработки и окружающей среды, последующее осуществление пиролиза путем косвенного нагрева при температуре 450-500°C подаваемым в реактор теплоносителем с отделением образующейся твердой фазы, разделением жидкой и парогазообразной фаз, содержащих углерод и углеводороды, и эвакуацию твердых субстанций пиролиза через шлюзовую камеру выгрузки, размещенную в нижней части реактора. Для пиролиза используют, по меньшей мере, один реактор, выполненный со сдвоенными стенками, в пространство между которыми осуществляют подачу предварительно разогретого теплоносителя. Теплоноситель подогревают посредством разогревающего котла, размещенного изолированно относительно реактора. Технический результат: обеспечение равномерности нагрева ...

device for thermal-catalytic decomposition - pyrolysis of organic waste materials

Device for Thermal-Catalytic Decomposition - Pyrolysis of Waste Organic Materials The specification relates to the device for thermal-catalytic decomposition - pyrolysis of waste organic materials, comprising: the reservoir, linked by means of the supply line with the reactor, where in the line is arranged the valve, wherein the reactor contains the heating element and/or the radiation source situated approximately up to the maximum level corresponding to 1/3 of the height from the bottom of the reactor; and the temperature sensor placed up to the maximum level corresponding to 1/3 of the height from the bottom of the reactor, wherein the output line protrudes from the lid of the reactor with the linked cooler, wherein the end of the output line is connected to the orifice on the receiver to contain liquefied products via the branch to exhaust product gases.

INDIRECTLY PYROLYSIS MECHANISM FOR PLASTIC WASTE HEATED

METHODS OF RECOVERING HYDROCARBONS FROM HYDROCARBONACEOUS MATERIAL USING A CONSTRUCTED INFRASTRUCTURE AND ASSOCIATED SYSTEMS MAINTAINED UNDER POSITIVE PRESSURE

A method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (100). This constructed infrastructure (100) defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body (120) of hydrocarbonaceous material. The permeable body (120) can be heated sufficient to remove hydrocarbons therefrom. During heating and removal of hydrocarbons and subsequent thereto a positive pressure can be maintained within the encapsulated volume by means of a non-oxidizing gas to expedite flushing of hydrocarbonaceous material, inhibit unwanted entry of oxygen into the encapsulated volume and remove recoverable hydrocarbons following the heating process.

Improvements in the manufacture and the purification of coke and apparatus used for this purpose

Methods of recovering hydrocarbons from hydrocarbonaceous material with reduced non-carbonaceous leachate and CO2 and associated systems

A method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a stationary permeability control infrastructure. This constructed infrastructure defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body of hydrocarbonaceous material. The permeable body can be heated sufficient to remove hydrocarbons therefrom within a temperature range which is sufficient to substantially avoid formation of carbon dioxide or non-hydrocarbon leachates. During heating the hydrocarbonaceous material is substantially stationary as the constructed infrastructure is a fixed structure. Removed hydrocarbons can be collected for further processing, use in the process, and/or use as recovered.

BIOMASS FRACTIONING PROCESS

A biomass fractionator and method are described for inputting ground biomass and outputting several vapor streams of bio-intermediate compounds along with syngas and biochar. In one embodiment, a method for biomass fractioning, comprises dispensing biomass into thin sheets of ground biomass; subjecting the thin sheets to ramps of temperature; and selectively collecting various groups of compounds as they are released from the thin sheets.

METHODS OF RECOVERING HYDROCARBONS FROM HYDROCARBONACEOUS MATERIAL USING A CONSTRUCTED INFRASTRUCTURE AND ASSOCIATED SYSTEMS

A method of recovering hydrocarbons from hydro carbonaceous materials can include forming a constructed permeability control infrastructure (100). Th is constructed infrastructure defines a substantially encapsulated volume. A comminuted hydro carbonaceous material can be introduced into the control i nfrastructure to form a permeable body (120) of hydro carbonaceous material. The permeable body (120) can be heated sufficient to remove hydrocarbons th erefrom such as by using heating conduits (118,126). During heating the hydr o carbonaceous material is substantially stationary as the constructed infra structure (100) is a fixed structure. Removed hydrocarbons can be collected as liquid products (136) and gaseous products (140) for further processing, use in the process, and/or use as recovered.

HIGH RANGE TEMPERATURE THERMAL DISMANTLING METHOD IN PROCESSING OIL SHALE

This invention consists of a new thermal dismantling method that enables reaching very high temperatures of 1000 oC for transforming any quality oil shale into directly refinable shale oil and to shale gas equal to natural gas, and as a by-product producing water and hot air, resulting in ash production where the ash is transformed into solid fuel by adding organic and non-organic additives and the residue of the burned solid fuel is used as raw material for other industrial products such as clinker, insulation material; by using its own solid fuel to raise and reach the high range temperature without the need to use any other type of fuel and without using water for the cooling system Oil shale is one of the rocks in which organic prong is mixed with widely variant of non-organic metal prong. This mixture contains a broad spectrum of mineral elements and it has the ability to generate all traditional sources of energy when treated by the thermal dismantling method. The thermal dismantling method is based on separating the volatile section which consists of shale gas, shale oil and water, the remaining section (the non-volatile section) is called the ash. The ash is taken, and then appropriate additive materials in specific quantities are added to it to produce the solid fuel. In such a way, it can be claimed that the following equation is maintained in an economic criteria and environmental standards: Oil shale = Solid Fuel + Crude oil + Natural Gas

APPARATUS AND METHOD FOR PYROLYZING COAL WITH WIDE PARTICLE SIZE DISTRIBUTION

A dry distillation device for coal with wide particle size distribution, a dry distillation device group and a dry distillation method based on the device. The device comprises a semicoke outlet (1), a combustion heating chamber (3), a coal feed port (5) and a pyrolysis gas discharge pipe (4). Two layers of division plates are disposed in the dry distillation device. A pyrolysis gas channel (2) is formed between the two layers of division plates, and holes are disposed on the division plate, so as to form a gas flow path from a fuel bed to the pyrolysis gas channel (2). Further, an internal component having fine heat transfer performance and made of a high-temperature-resistance material may be disposed in the dry distillation device, so as to strengthen heat transfer of a heating wall on the fuel bed and inside the fuel bed. Because the pyrolysis gas channel is added in the dry distillation reaction device, gaseous products generated in the coal dry distillation process can overflow in ...

METHODS TO RECOUP OF HYDRO-CARBONS OF MATERIAL HYDRO-CARBON BEING USED A CONSTRUCTED INFRASTRUCTURE AND SYSTEMS ASSOCIATES

A METHOD OF PYROLYSIS (THERMAL DECOMPOSITION) OF A SOLID BULK ORGANIC WASTE AND A REACTOR FOR PERFORMING THE METHOD

SYSTEM AND METHOD FOR BIOMASS FRACTIONING

A biomass fractionator and method are described for inputting ground biomass and outputting several vapor streams of bio-intermediate compounds along with syngas and biochar. In one embodiment, a method for biomass fractioning, comprises dispensing biomass into thin sheets of ground biomass; subjecting the thin sheets to ramps of temperature; and selectively collecting various groups of compounds as they are released from the thin sheets.

УТИЛИЗАЦИЯ ВЫСВОБОЖДАЕМЫХ СРЕДСТВ ИНДИВИДУАЛЬНОЙ ЗАЩИТЫ СПОСОБОМ БЕСКИСЛОРОДНОГО ТЕРМИЧЕСКОГО ПИРОЛИЗА

Изобретение относится к способам утилизации резиновых отходов средств индивидуальной защиты (СИЗ), а именно к разработке способа утилизации СИЗ (с истекшим сроком хранения). Способ утилизации резиновых отходов средств индивидуальной защиты (СИЗ) путем бескислородного термического пиролиза при температуре разложения СИЗ в интервале 700-800°С в лабораторной установке, содержащей: баллон с аргоном, реометр, лабораторный автотрансформатор, кварцевый реактор, решетку, электрическую печь, термопары, холодильник, сборник конденсата, потенциометр, газовый счетчик, паровой котел, при этом кварцевый реактор представляет собой цилиндрическую трубу диаметром 30 мм и высотой 250 мм, вертикально установленную в электрическую печь, отличающийся тем, что в состав лабораторной установки включен вакуумный насос, позволяющий снизить температуру разложения СИЗ до 500°С, уменьшить время проведения термического пиролиза и увеличить выход целевого продукта. Технический результат - снижение температуры термического ...

Holzkohleerzeuger für Kaminöfen

Holzkohleerzeuger für Kaminöfen

METHOD FOR PRODUCING NEGATIVE CARBON FUEL

A method and process is described for producing negative carbon fuel. In its broadest form, a carbon-containing input is converted to combustible fuels, refinery feedstock, or chemicals and a carbonaceous solid concurrently in separate and substantially uncontaminated form. I n an embodiment of the invent ion, biomass is converted via discrete increasing temperatures under pressure to blendable combustible fuels and a carbonaceous sol id. The carbonaceous sol id may be reacted to synthesis gas, sold as charcoal product, carbon credits, used for carbon offsets, or sequestered.

USE OF SPENT SHALE OR ASH OBTAINED FROM OIL SHALE DISMANTLING METHODS WITH OR WITHOUT ADDITIVES AS SOLID FUEL

In the present invention a method for producing solid fuel is developed. According to the method, spent shale, ash obtained by high temperature oil shale dismantling process, treated spent shale, ash obtained from direct burning of oil shale, ash obtained from indirect burning of oil shale or any mix of them is used as solid fuel without any additives or with organic and inorganic additives. The ignition temperature of the fuel is higher than 300°C, the speed of air flow in the burning chamber is higher than 5 m/s and oxygen may be added to improve burning efficiency during the burning process. In the present invention, methods for producing clinker, for producing raw material for manufacturing thermal isolation (insulation) materials, for producing raw material for manufacturing brick blocks as construction, for producing raw material for manufacturing pavement blocks and for producing active carbon for purification, filtering, adsorption and absorption of liquids and gases have been developed ...

SYSTEMS AND METHODS FOR RECYCLING PLASTIC

Systems and methods for recycling waste plastic can convert the waste plastic into a form of purified crude oil that includes one or more organic molecular species and that is free, or substantially free, of impurities such as acids and metals. In some systems and methods, the plastic is heated under vacuum conditions to effect depolymerization of the plastic, which yields a vapor, and the vapor is then directly contacted with a pH adjusted solution in a vapor treatment system. In some systems and methods, a continuous batch process is employed.

SYSTEMS AND METHODS FOR RECYCLING PLASTIC

Systems and methods for recycling waste plastic can convert the waste plastic into a form of purified crude oil that includes one or more organic molecular species and that is free, or substantially free, of impurities such as acids and metals. In some systems and methods, the plastic is heated under vacuum conditions to effect depolymerization of the plastic, which yields a vapor, and the vapor is then directly contacted with a pH adjusted solution in a vapor treatment system. In some systems and methods, a continuous batch process is employed.

PROCEDE D'OPTIMALISATION DU FONCTIONNEMENT D'UN FOUR DE COKEFACTION

L'INVENTION SE RAPPORTE AU DOMAINE DES FOURS DE COKEFACTION, ET EN PARTICULIER A LEUR REGULATION PAR MICROPROCESSEUR. LE PROCEDE SELON L'INVENTION, QUI VISE L'OPTIMALISATION DE LA COMBUSTION, LA REDUCTION DES PERTES EN GAZ DE CHEMINEE ET L'AMELIORATION DU RENDEMENT THERMIQUE, CONSISTE A REPARTIR EN SIX BLOCS DE FONCTIONS LES DIFFERENTS PARAMETRES INFLUANT SUR LE FONCTIONNEMENT DE L'INSTALLATION A FOURS DE COKEFACTION, C'EST-A-DIRE LES CARACTERISTIQUES DU GARNISSAGE, DU FOUR, DES GAZ ET DES CONDITIONS ATMOSPHERIQUES. CES BLOCS DE FONCTIONS SONT RELEVES, CALCULES ET EVALUES EN CONTINU PAR UN MICROPROCESSEUR QUI CORRIGE L'ALIMENTATION EN GAZ DE FOYER INFERIEUR EN FONCTION D'UN CERTAIN NOMBRE DE CRITERES PREDETERMINES TOUT EN ASSURANT UN REGLAGE STABLE. LORSQUE DES VALEURS LIMITES, L'UNE INFERIEURE, L'AUTRE SUPERIEURE, SONT DEPASSEES, LE SYSTEME EST SUSCEPTIBLE DE DECLENCHER L'ALERTE. LES VALEURS DE CONSIGNE PEUVENT ETRE MODULEES DE MANIERE CONTINUE OU DU MOINS ENDEANS CHAQUE CYCLE ENTIER, ...

METHODS OF RECOVERING HYDROCARBONS FROM HYDROCARBONACEOUS MATERIAL USING A CONSTRUCTED INFRASTRUCTURE HAVING PERMEABLE WALLS AND ASSOCIATED SYSTEMS

A method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure. This constructed infrastructure defines a substantially encapsulated volume having substantially permeable side walls and a substantially impermeable cap. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body of hydrocarbonaceous material. The permeable body can be heated sufficient to remove hydrocarbons therefrom without contamination or substantial leaching of materials outside of the impoundment. During heating the hydrocarbonaceous material is substantially stationary as the constructed infrastructure is a fixed structure. Removed hydrocarbons can be collected for further processing, use in the process, and/or use as recovered.

TYRE-MELTING MACHINE

Method and apparatus for the production of carbon fro carboniferous feedstock

A thermal dismantling unit and a high temperature furnace

This invention is related to a thermal dismantling unit that; " Reaches high temperatures (up to 3500oC), " Has been designed to be able to work with the three states (solid, liquid and gas) of fuel, " Works at low pressure by using a special vacuum circuit, " Bears a washing system in order to produce clean hot air suitable for domestic and industrial usage.

Method for producing negative carbon fuel

A method and process is described for producing negative carbon fuel. In its broadest form, a carbon-containing input is converted to combustible fuels, refinery feedstock, or chemicals and a carbonaceous solid concurrently in separate and substantially uncontaminated form. I n an embodiment of the invent ion, biomass is converted via discrete increasing temperatures under pressure to blendable combustible fuels and a carbonaceous sol id. The carbonaceous sol id may be reacted to synthesis gas, sold as charcoal product, carbon credits, used for carbon offsets, or sequestered.

APPARATUS AND METHOD FOR MAKING FUEL USING FOREST RESIDUE

Disclosed herein is an apparatus for producing fuel from forest residues, in which a variety of forest residues are sent from a first feeder (10) to a crusher (10), in which they are crushed, and the crushed material is subjected to intermediate processes and produced as standardized fuel in a pelletizer (35). The apparatus comprises: a second feeder (20), connected with both the downstream of the first feeder (10) and a mixer (15) and adapted to receive a second raw material for mixing with the first crushed raw material; a carbonizer (22) disposed downstream of the mixer (15) so as to receive an intermediate raw material and adapted to carbonize the intermediate raw material at high temperature and high speed; a crusher (26) disposed downstream of the carbonizer (22) so as to receive the carbonized intermediate material and adapted to crush the intermediate raw material, cooled in a cooler (24), into fine particles; and a third feeder (30) connected with both the downstream of the crusher (26) and a mixer (32) and adapted to receive a third raw material for mixing with the finely crushed intermediate raw material. Accordingly, the apparatus makes it convenient to transport, store and burn the biomass and can increase the heating value of combustion of the biomass, such that the biomass can provide an economic energy source.

APPARATUS AND METHOD FOR PYROLYZING COAL WITH WIDE PARTICLE SIZE DISTRIBUTION

A carbonization apparatus for coal with wide particle size distribution, a carbonization apparatus unit, and a carbonization method based on the apparatus. The apparatus comprises a char discharge outlet (1), a combustion heating chamber (3), a coal feeding inlet (5), and a pyrolysis gas exhausting pipe (4). Wherein, two partition plates between which a pyrolysis gas channel (2) is formed are further provided in the carbonization apparatus, and orifices are provided on the partition plates to form a gas flow path from the fuel bed to the pyrolysis gas channel (2). Further, another internal having good heat transfer performance and made of a material resistant to high temperature, is provided in this coal carbonization apparatus to enhance the heat transfer from the heated wall of the apparatus to the fuel bed inside the apparatus. With the pyrolysis gas channel in the carbonization reaction apparatus, the gaseous products generated from coal pyrolysis are enabled to flow out timely. Through providing the internals, it greatly improves the effects of heat and mass transfer and reduces the secondary reactions to increase the tar yield and quality.

INTERMEDIATE VAPOR COLLECTION WITHIN ENCAPSULATED CONTROL INFRASTRUCTURES

A method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (600). This constructed infrastructure (600) defines a substantially encapsulated volume. A mined hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body (605) of hydrocarbonaceous material. The permeable body (605) can be heated sufficient to remove hydrocarbons therefrom. Hydrocarbon products can be collected from intermediate locations (620, 630) within the permeable body (605). Advantageously, an intermediate fluid collection system (610) can be used to draw a hydrocarbon product from the permeable body (605) at preselected locations. Such intermediate collection can provide hydrocarbon product fractions which can reduce or eliminate the need for full-scale distillation of a hydrocarbon product having a full range of products such as that typically found in crude oil. In addition, product quality can ...

Methods of recovering hydrocarbons from hydrocarbonaceous material using a constructed infrastructure and associated systems

A method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure. This constructed infrastructure defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body of hydrocarbonaceous material. The permeable body can be heated sufficient to remove hydrocarbons therefrom. During heating the hydrocarbonaceous material is substantially stationary as the constructed infrastructure is a fixed structure. Removed hydrocarbons can be collected for further processing, use in the process, and/or use as recovered.

Methods of recovering hydrocarbons from hydrocarbonaceous material using a constructed infrastructure and associated systems maintained under positive pressure

A method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (100). This constructed infrastructure (100) defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body (120) of hydrocarbonaceous material. The permeable body (120) can be heated sufficient to remove hydrocarbons therefrom. During heating and removal of hydrocarbons and subsequent thereto a positive pressure can be maintained within the encapsulated volume by means of a non-oxidizing gas to expedite flushing of hydrocarbonaceous material, inhibit unwanted entry of oxygen into the encapsulated volume and remove recoverable hydrocarbons following the heating process.

Convective heat systems for recovery of hydrocarbons from encapsulated permeability control infrastructures

A constructed permeability control infrastructure (100) can include a permeability control impoundment, which defines a substantially encapsulated volume. The infrastructure (100) can also include a comminuted hydrocarbonaceous material within the encapsulated volume. The comminuted hydrocarbonaceous material can form a permeable body (120) of hydrocarbonaceous material. The infrastructure (100) can further include at least one convection driving conduit oriented in a lower portion of the permeable body (120) to generate bulk convective flow patterns throughout the permeable body (120). An associated method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (100), which defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure (100) to form a permeable body (120) of hydrocarbonaceous material. A heated fluid can be passed throughout ...

Carbon management and sequestration from encapsulated control infrastructures

A method of sequestering carbon dioxide emissions during recovery of hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (100). This constructed infrastructure (100) defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure (100) to form a permeable body (120) of hydrocarbonaceous material. The permeable body (120) can be heated sufficient to remove hydrocarbons therefrom. During heating, the hydrocarbonaceous material is substantially stationary as the constructed infrastructure (100) is a fixed structure. Additionally, during heating, any carbon dioxide that is produced can be sequestered. Removed hydrocarbons can be collected for further processing, use in the process, and/or use as recovered.

HYDROCARBON CONVERSION PROCESS

The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.

METHOD FOR PRODUCING NEGATIVE CARBON FUEL

A method and process is described for producing negative carbon fuel. In its broadest form, a carbon-containing input is converted to combustible fuels, refinery feedstock, or chemicals and a carbonaceous solid concurrently in separate and substantially uncontaminated form. I n an embodiment of the invent ion, biomass is converted via discrete increasing temperatures under pressure to blendable combustible fuels and a carbonaceous sol id. The carbonaceous sol id may be reacted to synthesis gas, sold as charcoal product, carbon credits, used for carbon offsets, or sequestered.

SYSTEM AND METHOD FOR BIOMASS FRACTIONING

A biomass fractionator and method are described for inputting ground biomass and outputting several vapor streams of bio-intermediate compounds along with syngas and biochar. In one embodiment, a method for biomass fractioning, comprises dispensing biomass into thin sheets of ground biomass; subjecting the thin sheets to ramps of temperature; and selectively collecting various groups of compounds as they are released from the thin sheets.

RECYCLING OF TIRES, RUBBER AND OTHER ORGANIC MATERIAL THROUGH VAPOR DISTILLATION

A processor for vacuum distillation of whole tires including: an insulated housing having a door on one end, a central radiant heat tube and a plurality of peripheral heat tubes spaced about the central radiant heat tube and arranged with an inlet leg of each peripheral heat tube adjacent an outlet leg of another peripheral heat tube to maximize utilization of the radiant heat energy from the peripheral heat tubes. The central radiant heat tube has an unsupported end adjacent the door such that the tires loaded through door will pass over the central radiant heat tube and such that the central radiant heat tube is in a central opening of each tire.

SYSTEMS AND METHODS FOR RECYCLING PLASTIC

Systems and methods for recycling waste plastic can convert the waste plastic into a form of purified crude oil that includes one or more organic molecular species and that is free, or substantially free, of impurities such as acids and metals. In some systems and methods, the plastic is heated under vacuum conditions to effect depolymerization of the plastic, which yields a vapor, and the vapor is then directly contacted with a pH adjusted solution in a vapor treatment system. In some systems and methods, a continuous batch process is employed.

Convective heat systems for recovery of hydrocarbons from encapsulated permeability control infrastructures

A constructed permeability control infrastructure can include a permeability control impoundment, which defines a substantially encapsulated volume. The infrastructure can also include a comminuted hydrocarbonaceous material within the encapsulated volume. The comminuted hydrocarbonaceous material can form a permeable body of hydrocarbonaceous material. The infrastructure can further include at least one convection driving conduit oriented in a lower portion of the permeable body to generate bulk convective flow patterns throughout the permeable body. An associated method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure, which defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body of hydrocarbonaceous material. A heated fluid can be passed throughout the permeable body in bulk convective flow patterns to ...

Pyrolysis reactor system for the conversion and analysis of organic solid waste

The pyrolysis reactor system for the conversion and analysis of organic solid waste is a dual gas-liquid separation system, allowing for the conversion of organic solid waste, as well as analysis of the conversion products. A pyrolysis reactor is provided for converting the organic solid waste into a solid product and a gas-liquid product mixture through pyrolysis. A source of carrier gas is in fluid communication with the pyrolysis reactor for degrading the organic solid waste. A first gas-liquid separator is in fluid communication with the pyrolysis reactor and receives the gas-liquid product mixture therefrom, separating a portion of gas therefrom. A second gas-liquid separator is in fluid communication with the first gas-liquid separator and receives the gas-liquid product mixture therefrom and separates the remainder of the gas therefrom. The remainder of the gas and the separated liquid are each collected separately from one another, in addition to the char.

Dry distillation device and method for coal with wide particle size distribution

A dry distillation device for coal with wide particle size distribution, a dry distillation device group and a dry distillation method based on the device. The device comprises a semicoke outlet (1), a combustion heating chamber (3), a coal feed port (5) and a pyrolysis gas discharge pipe (4). Two layers of division plates are disposed in the dry distillation device. A pyrolysis gas channel (2) is formed between the two layers of division plates, and holes are disposed on the division plate, so as to form a gas flow path from a fuel bed to the pyrolysis gas channel (2). Further, an internal component having fine heat transfer performance and made of a high-temperature-resistance material may be disposed in the dry distillation device, so as to strengthen heat transfer of a heating wall on the fuel bed and inside the fuel bed. Because the pyrolysis gas channel is added in the dry distillation reaction device, gaseous products generated in the coal dry distillation process can overflow in time. At the same time, by disposing the internal component, heat and mass transfer effects are improved, a secondary reaction is reduced, and tar yield and quality are further improved.

Intermediate vapor collection within encapsulated control infrastructures

A method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (600). This constructed infrastructure (600) defines a substantially encapsulated volume. A mined hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body (605) of hydrocarbonaceous material. The permeable body (605) can be heated sufficient to remove hydrocarbons therefrom. Hydrocarbon products can be collected from intermediate locations (620, 630) within the permeable body (605). Advantageously, an intermediate fluid collection system (610) can be used to draw a hydrocarbon product from the permeable body (605) at preselected locations. Such intermediate collection can provide hydrocarbon product fractions which can reduce or eliminate the need for full-scale distillation of a hydrocarbon product having a full range of products such as that typically found in crude oil. In addition, product quality can ...

INDIRECTLY HEATED WASTE PLASTIC PYROLYSIS DEVICE

A THERMAL DISMANTLING UNIT AND A HIGH TEMPERATURE FURNACE

This invention is related to a thermal dismantling unit that; " Reaches high temperatures (up to 3500oC), " Has been designed to be able to work with the three states (solid, liquid and gas) of fuel, " Works at low pressure by using a special vacuum circuit, " Bears a washing system in order to produce clean hot air suitable for domestic and industrial usage.

CONVECTIVE HEAT SYSTEMS FOR RECOVERY OF HYDROCARBONS FROM ENCAPSULATED PERMEABILITY CONTROL INFRASTRUCTURES

A constructed permeability control infrastructure (100) can include a permeability control impoundment, which defines a substantially encapsulated volume. The infrastructure (100) can also include a comminuted hydrocarbonaceous material within the encapsulated volume. The comminuted hydrocarbonaceous material can form a permeable body (120) of hydrocarbonaceous material. The infrastructure (100) can further include at least one convection driving conduit oriented in a lower portion of the permeable body (120) to generate bulk convective flow patterns throughout the permeable body (120). An associated method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (100), which defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure (100) to form a permeable body (120) of hydrocarbonaceous material. A heated fluid can be passed throughout ...

Process for the treatment and the transformation of fuels

PROCESS AND ENGINE FOR THE GASIFICATION OF THE BIOMASS AND THE DECHETSBIOLOGIQUES

PROCESS Of OPTIMIZATION OF the OPERATION Of a FURNACE OF COKING

INDIRECTLY HEATED WASTE PLASTIC PYROLYSIS DEVICE

The invention subject is device to pyrolysis waste plastics, operated under normal, high or low pressure, membrane heated. The device character, according to the invention is that reactor (1) is equipped with inside reaction chamber at least one heating element as heating pipe (7) of curve shape and it's length to diameter ratio is at least 10, beneficially 50-250, and the heating pipe (7) is supported by at least one support (22) and on the inlet end of the heating pipe (7) a burner (13) is fixed.

INDIREKT BEHEIZTE PYROLYSEEINRICHTUNG FÜR KUNSTSTOFFABFALL

Verfahren und Vorrichtung zur Herstellung von Aktivkohle unter Verwendung von kohlehaltigem Material

Method of optimising the operation of coke ovens

PROCESS FOR VACUUM PYROLYSIS REMOVAL OF POLYMERS FROM VARIOUS OBJECTS

Hydrocarbon conversion method

Process and distilling apparatus of solid fuels, the bituminous and the resins and rosins, and proceeded schists of recovery of the hydrogen sulphide, benzole and other carbides volatile, while deriving

CONVECTIVE HEAT SYSTEMS FOR RECOVERY OF HYDROCARBONS FROM ENCAPSULATED PERMEABILITY CONTROL INFRASTRUCTURES

A constructed permeability control infrastructure (100) can include a permeability control impoundment, which defines a substantially encapsulated volume. The infrastructure (100) can also include a comminuted hydrocarbonaceous material within the encapsulated volume. The comminuted hydrocarbonaceous material can form a permeable body (120) of hydrocarbonaceous material. The infrastructure (100) can further include at least one convection driving conduit oriented in a lower portion of the permeable body (120) to generate bulk convective flow patterns throughout the permeable body (120). An associated method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (100), which defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure (100) to form a permeable body (120) of hydrocarbonaceous material. A heated fluid can be passed throughout ...

METHOD AND APPARATUS FOR THE PRODUCTION OF CARBON FRO CARBONIFEROUS FEEDSTOCK

The present invention is directed apparatus for producing a carbon product from carboniferous material, such materials including wood and other green waste, various biomass, and waste materials such as tyres and plastics. A reaction chamber of specific characteristics heats the carboniferous feedstock to a threshold temperature to initiate a process of carbonisation to yield a carbon product. The apparatus is adaptable to continuous and semi-continuous processing of feedstock.

Verfahren und Anlage zur thermischen Verwertung von Abfaellen

METHOD OF DESTRUCTING REFUSE AND OTHER WASTE PRODUCTS

... 1286595 Gasifying refuse K K K KROYER 19 April 1971 [5 Feb 1970] 5540/70 Heading C5E A method of destructing refuse, e.g. chlorinecontaining polymers, which on pyrolysing produces acidic gases, comprises pyrolysing the refuse at a temperature between 700‹ and 1200‹ C. in an externally heated furnace from which the gases are recovered as fuel gases, and continuously determining the acidity of the gases, e.g. by measuring the pH of an aqueous solution used for washing them, and introducing into the furnace alkaline reacting products or products forming alkaline reacting compounds on being pyrolized, in amounts which neutralize the acidic reaction of the gases. The added product may be lime or kitchen waste or offal.

APPARATUS AND METHOD FOR MAKING FUEL USING FOREST RESIDUE

Disclosed herein is an apparatus for producing fuel from forest residues, in which a variety of forest residues are sent from a first feeder (10) to a crusher (10), in which they are crushed, and the crushed material is subje cted to intermediate processes and produced as standardized fuel in a pellet izer (35). The apparatus comprises: a second feeder (20), connected with bot h the downstream of the first feeder (10) and a mixer (15) and adapted to re ceive a second raw material for mixing with the first crushed raw material; a carbonizer (22) disposed downstream of the mixer (15) so as to receive an intermediate raw material and adapted to carbonize the intermediate raw mate rial at high temperature and high speed; a crusher (26) disposed downstream of the carbonizer (22) so as to receive the carbonized intermediate material and adapted to crush the intermediate raw material, cooled in a cooler (24) , into fine particles; and a third feeder (30) connected with both the downs tream of ...

CARBON MANAGEMENT AND SEQUESTRATION FROM ENCAPSULATED CONTROL INFRASTRUCTURES

A method of sequestering carbon dioxide emissions during recovery of hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (100). This constructed infrastructure (100) defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure (100) to form a permeable body (120) of hydrocarbonaceous material. The permeable body (120) can be heated sufficient to remove hydrocarbons therefrom. During heating, the hydrocarbonaceous material is substantially stationary as the constructed infrastructure (100) is a fixed structure. Additionally, during heating, any carbon dioxide that is produced can be sequestered. Removed hydrocarbons can be collected for further processing, use in the process, and/or use as recovered.

SYSTEM AND METHOD FOR BIOMASS FRACTIONING

A biomass fractionator and method are described for inputting ground biomass and outputting several vapor streams of bio-intermediate compounds along with syngas and biochar. In one embodiment, a method for biomass fractioning, comprises dispensing biomass into thin sheets of ground biomass; subjecting the thin sheets to ramps of temperature; and selectively collecting various groups of compounds as they are released from the thin sheets.

Device for utilizing steel slag waste heat and waste biological resources to produce charcoal

METHOD AND APPARATUS FOR THE PRODUCTION OF CARBON FRO CARBONIFEROUS FEEDSTOCK

The present invention is directed apparatus for producing a carbon product from carboniferous material, such materials including wood and other green waste, various biomass, and waste materials such as tyres and plastics. A reaction chamber of specific characteristics heats the carboniferous feedstock to a threshold temperature to initiate a process of carbonisation to yield a carbon product. The apparatus is adaptable to continuous and semi-continuous processing of feedstock.

Hydrocarbon conversion process

The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.

Hydrocarbon Conversion Process

The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.

Hydrocarbon Conversion Process

The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes. 1. A regenerative , reverse-flow pyrolysis reactor comprising ,(a) first and second reactors, each comprising a unitary reactor bed;(b) a mixing region located between the first and second reactors;(c) first and second channels located within the first reactor, the first and second channels being thermally-connected, substantially independent flow-paths;(d) a third channel located within the second reactor; and (i) a first reactant via the first channel during a first time interval,', '(ii) a second reactant via a second channel during the first time interval, and', '(iii) a first portion of the second reactant via the first channel and a second portion of the second reactant via the second channel during a second time interval., '(e) first valve means for directing to the mixing region'}2. The regenerative claim 1 , reverse-flow pyrolysis reactor of claim 1 , further comprising second valve means for directing a hydrocarbon-containing feed to the second reactor for pyrolysis.3. The regenerative claim 1 , reverse-flow pyrolysis reactor of claim 1 , wherein at least one of the first or second valve means comprises hydrodynamic valve means including at least one sparger.4. A process for removing combustible non-volatiles from a reactor system claim 1 , comprising:(A) depositing combustible non-volatiles during a first conversion step, the combustible non-volatiles being deposited in first and second conduits of a first reactor, the first reactor being located within the reactor system; (a) conducting a first-reactant through the first conduit and a second-reactant through the second conduit;', '(b) heating the reactor system by exothermically reacting at least a portion of the ...

Carbonization/oil recovery treatment furnace

There is provided a carbonization/oil recovery processing furnace which can be manufactured at a relatively low cost and has less deterioration due to corrosion in association with operation, and can also be maintained and managed at low cost. The carbonization/oil recovery processing furnace is constituted so as to process discarded materials including plastic waste by carbonization and oil recovery with the use of superheated steam which is supplied from the outside, and the carbonization/oil recovery processing furnace is constituted of iron-made external structures and stainless steel-made internal structures which can be separated from the external structures.

CARBONIZED MATERIAL PRODUCTION KILN

To enable a carbonized material production kiln to be maintained in a simple manner when an exposed surface on a side wall of the kiln is cracked, to prevent the kiln from easily cracking by heat to thereby prolong the life of the kiln itself, and to increase heat retention efficiency to thereby increase carbonization efficiency even during periods of cold temperatures such as the winter season. The carbonized material production kiln is formed by stacking cubic concrete blocks each having no reinforcing iron so that recombination of up to six faces of each cubic concrete block becomes possible, wherein a heat storage/retention member such as stones is filled in an exhaust space formed between a kiln floor iron plate and a kiln bottom so as to store heat, thereby preventing a decrease in carbonization efficiency even at cold temperatures. 1. A carbonized material production kiln including an open ceiling surface , side walls at four faces being in a quadrangular shape , an exhaust space which is formed between an iron plate with a vent hole opened that is laid as a kiln floor in a state of being enclosed by the side walls and a kiln bottom surface and through which exhaust gas discharged as a result of carbonization of a raw material for carbonization , a combustion device being made to communicate with the discharge space and for combusting exhaust gas , and a stage which is continuous to at least one side wall of the side walls and on which a traveling work machine can travel at the same height as that of an upper surface of the side wall , wherein for repeatedly performing making a moisture percentage of a raw material for carbonization to be loaded into the production kiln be that in an unseasoned wood state to cause a film of steam generated with accelerated carbonization of the raw material for carbonization to shut off outside air , pressing an upper surface of the raw material for carbonization loaded in the production kiln into a state of an outside air ...

HIGH RANGE TEMPERATURE THERMAL DISMANTLING METHOD IN PROCESSING OIL SHALE

This invention consists of a new thermal dismantling method that enables reaching very high temperatures of 1000° C. for transforming any quality oil shale into directly refinable shale oil and to shale gas equal to natural gas, and as a by-product producing water and hot air, resulting in ash production where the ash is transformed into solid fuel by adding organic and non-organic additives and the residue of the burned solid fuel is used as raw material for other industrial products such as clinker, insulation material; by using its own solid fuel to raise and reach the high range temperature without the need to use any other type of fuel and without using water for the cooling system. 1- A high range temperature thermal dismantling method conducted in between 850° C. and 1000° C. in processing oil shale , bituminous sand in order to obtain shale gas which matches the specifications of the natural gas , shale oil which is consistent in specifications , structural and chemical composition with the crude oil , so that it can be sent directly to the crude oil refineries without need for specific treatment or hydrogenation process , whereinthe dismantling process is conducted in a reactor positioned inside a furnace in which solid fuel which is oil shale ash taken out of the reactor and cooled and then treated is burned indirectly to heat oil shale placed inside the reactor,shale gas, shale oil, water, purified hot air are extracted separately during dismantling process,shale gas and water vapour are separated by using vacuum pump to be directed into condenser, after the condenser the shale oil and the water are liquidised while the gas has been directed to gas tank,shale oil is separated from the water by using separation tower and water is directed to the water tank,the hot air is pulled from the furnace and directed to the washing and cleaning unit, after that the hot air is directed to the heat exchange and precipitator unit, andthe resulting oil shale ash from ...

Hydrocarbon Conversion Process

The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.

Hydrocarbon conversion process

The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.

一种有机质微波热解炭化装置

本发明公开了一种有机质微波热解炭化装置，涉及热解炭化技术领域。本发明包括炉体、炉盖以及载物框，炉盖一侧面通过铰座与炉体顶部铰接，炉盖一表面对称固定连接有两个吊杆，吊杆一侧面开设有销孔，载物框顶部对称固定连接有两个弹性竖板，弹性竖板一侧面固定有插销，插销一端与销孔内壁转动配合，两个弹性竖板侧面之间固定连接有限位弹簧，弹性竖板上端的周侧面固定连接有绝热层。本发明通过炉盖、载物框、吊杆、弹性竖板、插销和绝热层的设计，结构简单，加快了炭化后的原料冷却速度，避免了现有的微波热解炭化装置不方便取放原料，炭化后的原料在装置内冷却速度较慢，浪费时间，影响实验研究进程的问题。

The biomass microwave catalytic pyrolysis method and its integrated apparatus of catalyst regeneration

本发明公开了一种催化剂再生的生物质微波催化热解方法及其一体化装置。所述方法包括如下步骤：生物质进入热解区进行热解反应后生成的固体残留物成为生物炭，热解气经生物炭层脱除焦油，进入放置有催化剂的催化区，进行进一步的裂解催化。热解区、焦油脱除区、催化重整区和催化剂再生区主要由微波加热装置供热，而催化剂再生区向外辐射的热量作为辅助供热。热解区、焦油脱除区、催化重整区接收辐射的热量，保证热解区、焦油脱除区、催化重整区快速、稳定达到设定温度。所述一体化装置将普遍分离的催化热解与催化剂再生两个过程联系在同一套装置内，实现热量的分级利用、能量利用效率高、节能环保，可广泛地适用于生物质热解领域，应用前景较广。

Method for call waiting service in video telecommunication network

본 발명은 화상 호 교환을 수행하는 교환기와, 가입자 정보 및 통화 대기 서비스 가입 여부 정보를 저장하는 가입자 정보 서버를 포함하는 화상 전화망에의 통화 대기 서비스 방법에 관한 것이다. 본 발명의 통화 대기 서비스 방법은, 제1단말과 제2단말 간 화상 통화 중, 제3단말로부터 상기 제1단말로 호가 시도됨에 따라 제3교환기로부터 제1교환기로 착신이 요청되면, 상기 제1교환기가 상기 가입자 정보 서버를 통해 상기 제1단말이 통화 대기 서비스 가입자 단말인지의 여부를 판단하는 제1단계와; 상기 판단 결과, 제1단말이 통화 대기 서비스 가입자 단말인 경우, 상기 제1교환기가 상기 제1단말의 화면에 디스플레이하기 위한 상기 제3단말과의 통화 연결 메뉴, 제3단말의 호 대기 메뉴, 착신 불능 안내 메시지 전송 메뉴를 포함하는 착신 요청 텍스트 메시지를 전송하는 제2단계와; 상기 제1단말로부터 상기 착신 요청 텍스트 메시지에 대한 응답으로 특정 메뉴를 선택하는 디지트가 전송되면, 해당 선택 메뉴에 따라 제1단말과 제3단말과의 통화 연결, 제3단말의 호 대기, 제3단말로의 착신 불능 안내 메시지 전송 중 어느 하나를 수행하는 제3단계; 를 포함하여 이루어짐에 기술적 특징이 있다. The present invention relates to a call waiting service method for a video telephone network including a switch performing a video call exchange and a subscriber information server storing subscriber information and call subscription service subscription information. In the call waiting service method of the present invention, when a call is requested from a third exchange to a first exchange as a call is attempted from a third terminal to a first terminal during a video call between the first terminal and the second terminal, A first step of the exchange determining whether the first terminal is a call waiting service subscriber terminal through the subscriber information server; As a result of the determination, when the first terminal is a call waiting service subscriber terminal, the call exchange menu with the third terminal for displaying on the screen of the first terminal by the first exchange, a call waiting menu with the third terminal, and the call Transmitting a call request text message including a disable guide message transmission menu; When a digit for selecting a specific menu is transmitted in response to the incoming request text message from the first terminal, a call connection between the first terminal and the third terminal, a call waiting of the third terminal, and a third terminal are selected according to the selection menu. A third step of ...

Hydrocarbon conversion process

本发明涉及将烃成为不饱和产物诸如乙炔和/或乙烯的方法。本发明也涉及将乙炔转化至烯烃比如乙烯和/或丙烯，涉及聚合该烯烃、以及涉及用于这些方法的设备。

System and method for continuous production of a renewable liquid fuel

A system and method for torrefying a combination of biomass and biochar colloidal dispersion is provided.

Carbon management and sequestration from encapsulated control infrastructures

本发明涉及一种在从含烃材料回收烃期间截存二氧化碳排放的方法，该方法可以包括形成构造化渗透性控制基层结构(100)。该构造化基层结构(100)限定基本密闭体积。粉碎的含烃材料可以被引入该控制基层结构(100)以形成含烃材料的可渗透体(120)。可渗透体(120)可以充分加热以从其中去除烃。在加热期间，由于构造化基层结构(100)是固定结构，因此含烃材料基本静止。另外，在加热期间，可以截存产生的任何二氧化碳。去除的烃可以被收集用以进一步加工、在处理中使用和/或在回收时使用。

System and method for biomass fractioning

A biomass fractionator and method are described for inputting ground biomass and outputting several vapor streams of bio-intermediate compounds along with syngas and biochar. In one embodiment, a method for biomass fractioning, comprises dispensing biomass into thin sheets of ground biomass; subjecting the thin sheets to ramps of temperature; and selectively collecting various groups of compounds as they are released from the thin sheets.

Method for producing negative carbon fuel

A method and process is described for producing negative carbon fuel. In its broadest form, a carbon-containing input is converted to combustible fuels, refinery feedstock, or chemicals and a carbonaceous solid concurrently in separate and substantially uncontaminated form. In an embodiment of the invention, biomass is converted via discrete increasing temperatures under pressure to blendable combustible fuels and a carbonaceous solid. The carbonaceous solid may be reacted to synthesis gas, sold as charcoal product, carbon credits, used for carbon offsets, or sequestered.

Staged biomass fractionator

Various biomass reactors systems and methods of pyrolyzing biomass are disclosed. One type of biomass reactor system comprises a plurality of biomass processing stations configured in series, each station comprising an auger reactor including an auger inlet for receiving biomass and a transfer screw for conveying the biomass through the auger reactor.

System and method for biomass fractioning

A biomass fractionator and method are described for inputting ground biomass and outputting several vapor streams of bio-intermediate compounds along with syngas and biochar. A method for biomass fractioning comprises dispensing biomass into thin sheets of ground biomass; subjecting the thin sheets to ramps of temperature; and selectively collecting various groups of compounds as they are released from the thin sheets.

System and method for biomass fractioning

A biomass fractionator and method are described for inputting ground biomass and outputting several vapor streams of bio-intermediate compounds along with syngas and biochar. In particular, a method for biomass fractioning, comprises dispensing biomass into thin sheets of ground biomass; subjecting the thin sheets to ramps of temperature; and selectively collecting various groups of compounds as they are released from the thin sheets.

Method for producing negative carbon fuel

A method and process is described for producing negative carbon fuel. In its broadest form, a carbon-containing input is converted to combustible fuels, refinery feedstock, or chemicals and a carbonaceous solid concurrently in separate and substantially uncontaminated form. In an embodiment of the invention, biomass is converted via discrete increasing temperatures under pressure to blendable combustible fuels and a carbonaceous solid. The carbonaceous solid may be reacted to synthesis gas, sold as charcoal product, carbon credits, used for carbon offsets, or sequestered.

Method for making sequesterable biochar

A method and process is described for producing negative carbon fuel. In its broadest form, a carbon-containing input is converted to combustible fuels, refinery feedstock, or chemicals and a carbonaceous solid concurrently in separate and substantially uncontaminated form. In an embodiment of the invention, biomass is converted via discrete increasing temperatures under pressure to blendable combustible fuels and a carbonaceous solid. The carbonaceous solid may be reacted to synthesis gas, sold as charcoal product, carbon credits, used for carbon offsets, or sequestered.

Method for producing negative carbon fuel

A method and process is described for producing negative carbon fuel. In its broadest form, a carbon-containing input is converted to combustible fuels, refinery feedstock, or chemicals and a carbonaceous solid concurrently in separate and substantially uncontaminated form. In an embodiment of the invention, biomass is converted via discrete increasing temperatures under pressure to blendable combustible fuels and a carbonaceous solid. The carbonaceous solid may be reacted to synthesis gas, sold as charcoal product, carbon credits, used for carbon offsets, or sequestered.

System and method for biomass fractioning

A biomass fractionator and method are described for inputting ground biomass and outputting several vapor streams of bio-intermediate compounds along with syngas and biochar. In one embodiment, a method for biomass fractioning, comprises dispensing biomass into thin sheets of ground biomass; subjecting the thin sheets to ramps of temperature; and selectively collecting various groups of compounds as they are released from the thin sheets.

Method for producing carbonized material using garbage without causing pollution by eco-friendly process

본 발명은 친환경으로 환경오염이 발생되지 않는 음식물찌꺼기를 이용한 탄화재생산방법에 관한 것으로서, 환경오염을 최소화 시키면서 환경오염의 원인인 음식물찌꺼기를 처리하고, 음식물찌꺼기를 연료로 사용할 수 있는 탄화재를 생산하여 탄화처리과정에서 악취 발생이나 다이옥신과 같은 오염물질의 배출을 방지하도록 다단계의 정화처리과정 및 급생시킴으로 응축시킬 수 있는 처리 방법을 수행하여 환경오염을 방지할 수 있는 뛰어난 효과가 있는 매우 유용한 발명인 것이다. 음식물찌꺼기, 탄화, 친화경, 재활용

Use of spent shale or ash obtained from oil shale dismantling methods with or without additives as solid fuel

IMPROVEMENTS IN APPARATUS FOR THE MANUFACTURE OF CARBON BISULFIDE

Perfeccionamientos en aparatos para la fabricación de bisulfuro de carbono caracterizados por una retorta que comprende; una cámara de reacción; una cámara exterior de caldeo previo que rodea la cámara de reacción y comunica con ella por un extremo; medios para suministrar azufre a la cámara de caldeo previo; material inerte de relleno en el interior de la cámara de caldeo previo; para favorecer la transmisión de calor al azufre; medios para introducir material carbonoso en la cámara de reacción y medios para retirar de la cámara de reacción a medida que se forman los vapores de bisulfuro de carbono. Improvements in devices for the manufacture of carbon disulfide characterized by a retort comprising; a reaction chamber; an external pre-heating chamber that surrounds the reaction chamber and communicates with it at one end; means for supplying sulfur to the preheat chamber; inert filling material inside the pre-heating chamber; to favor the transfer of heat to the sulfur; means for introducing carbonaceous material into the reaction chamber and means for withdrawing from the reaction chamber as carbon disulfide vapors are formed.

Low temperature continuous pyrolysis biomass prepare fixed bed reactors and the method for activated carbon

本发明涉及低温连续热解生物质制备活性炭的固定床反应器及方法。本发明所述反应器包括进料口、反应系统、出料口，进料口在出料口之上，反应系统自上而下包括集气室、气体收集区、反应室；反应室中具有进料螺旋、出料螺旋、料板，料板包括进料端和出料端，进料螺旋在进料口之下、进料端上部，出料螺旋在出料端上部，出料端在出料口之上，进料螺旋包括中心螺杆和左、右螺旋叶片，左、右螺旋叶片被中心螺杆横穿，且垂直于中心螺杆的中心线成轴对称，距离为进料口口径的1/3～1/2；反应室具有反应室隔板，两端分别连接蒸汽入口和蒸汽喷嘴，用于向反应室中喷入蒸汽。本发明所述反应器可同时实现生物质的热解和活性炭的制备，可连续进出料，经济效益显著。

A kind of large-scale pyrolysis installation

本发明提供了一种大型热解装置，技术方案是：最内侧的换热管形成物料通道，相邻换热管的间距从进料端到出料端逐渐变小，以形成从进料端到出料端孔径逐渐变大的锥形的物料通道；送料装置为带有空心轴的套筒式螺旋进料装置，该空心轴与筒体的内腔联通。由于换热管间距根据据物料在热解窑内不同阶段的体积变化、流动性变化来确定，物料在热解窑内各个部分均可形成高效换热料幕。同时，出料端也是高温端，缩小出料端的直径，从而使出料罩处筒体回转直径小，便于制作可靠性高、泄漏量小的耐高温密封装置，同时设置空心轴可以根据工艺需要，将筒体内的水蒸气抽出或添加净化煤气，以满足工艺需求。

Use of spent shale or ash obtained from oil shale dismantling methods with or without additives as solid fuel

In the present invention a method for producing solid fuel is developed. According to the method, spent shale, ash obtained by high temperature oil shale dismantling process, treated spent shale, ash obtained from direct burning of oil shale, ash obtained from indirect burning of oil shale or any mix of them is used as solid fuel without any additives or with organic and inorganic additives. The ignition temperature of the fuel is higher than 300°C, the speed of air flow in the burning chamber is higher than 5 m/s and oxygen may be added to improve burning efficiency during the burning process. In the present invention, methods for producing clinker, for producing raw material for manufacturing thermal isolation (insulation) materials, for producing raw material for manufacturing brick blocks as construction, for producing raw material for manufacturing pavement blocks and for producing active carbon for purification, filtering, adsorption and absorption of liquids and gases have been developed to improve burning efficiency during the burning process.

Carbonization coupling coal fired power plants before a kind of stalk external combustion fair current bed furnace

本发明公开了一种秸秆外燃顺流固定床炉前碳化耦合燃煤发电装置，包括输送机、给料机、锁气器、主料仓、碳化室、布气室、排渣室、集气器、换热器、四通阀、第一循环风机、燃烧器、燃烧室、点火燃烧器、调温室、第二循环风机、风机、第四循环风机、监测单元；输送机经给料机与锁气器相连；锁气器经碳化室与排渣室相连；碳化室连接换热器；换热器连接四通阀；四通阀的第一出口经第一循环风机连接燃烧器；风机连接燃烧器；燃烧器与燃烧室相连；燃烧室与调温室相连；调温室出口连接碳化室；四通阀第二出口经第二循环风机与调温室相连；四通阀第三出口与第三循环风机相连；循环风机与电站锅炉相连；监测单元监测燃烧室、调温室出口的温度；本装置解决了结渣和腐蚀问题。

Hydrocarbon conversion process

The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.

CONVECTIVE HEAT SYSTEMS FOR THE RECOVERY OF HYDROCARBONS FROM ENCAPSULATED PERMEABILITY CONTROL INFRASTRUCTURE

REFERIDO A UNA INFRAESTRUCTURA DE CONTROL DE PERMEABILIDAD CONSTRUIDA, QUE COMPRENDE: a) UN EMBALSE DE CONTROL DE PERMEABILIDAD QUE DEFINE UN VOLUMEN SUSTANCIALMENTE ENCAPSULADO; b) UN MATERIAL HIDROCARBONACEO TRITURADO DENTRO DEL VOLUMEN ENCAPSULADO QUE FORMA UN CUERPO PERMEABLE DEL MATERIAL HIDROCARBONACEO; Y c) AL MENOS UN CONDUCTO IMPULSOR POR CONVECCION ORIENTADO A UNA PORCION INFERIOR DEL CUERPO PERMEABLE PARA GENERAR PATRONES DE FLUJO CONVECTIVO DE MASA EN TODO EL CUERPO PERMEABLE REFERRED TO A CONSTRUCTED PERMEABILITY CONTROL INFRASTRUCTURE, INCLUDING: a) A PERMEABILITY CONTROL RESERVOIR DEFINING A SUBSTANTIALLY ENCAPSULATED VOLUME; b) A HYDROCARBONACEOUS MATERIAL CRUSHED WITHIN THE ENCAPSULATED VOLUME THAT FORMS A PERMEABLE BODY OF THE HYDROCARBONACEOUS MATERIAL; AND c) AT LEAST ONE DRIVING DUCT BY CONVECTION ORIENTED TO A LOWER PORTION OF THE PERMEABLE BODY TO GENERATE CONVECTIVE MASS FLOW PATTERNS THROUGHOUT THE PERMEABLE BODY.

Carbide generation kiln

課題は、炭化物生成窯において、側壁の露出面がひび割れたりしたような場合に簡単にメンテナンスができると共に、熱により割れづらくして窯自体の長寿命化を図り、さらに熱保持効率を高めて冬季等の寒いときにおいても炭化効率を高めることである。 解決手段は、炭化物生成窯を、鉄筋のない立方体形状のコンクリートブロックを積層して形成して最大６面の組み換えができるようにすると共に、窯床鉄板５と窯底４とのあいだの排気空間Ｓに石等の蓄熱保持部材7を充填して蓄熱できるようにして寒いときでも炭化効率が低下しないようにする事である。 The problem is that in the case of a carbide generation kiln, when the exposed surface of the side wall is cracked, it can be easily maintained, and it is hard to crack due to heat, extending the life of the kiln itself, and further increasing the heat retention efficiency in winter. It is to increase carbonization efficiency even when it is cold. The solution is that a carbide generating kiln is formed by stacking cube-shaped concrete blocks without reinforcing bars so that up to six surfaces can be recombined, and an exhaust space between the kiln floor iron plate 5 and the kiln bottom 4 is provided. The heat storage holding member 7 such as stone is filled in S so that heat can be stored so that the carbonization efficiency does not decrease even when it is cold.

Methods of recovering hydrocarbons from hydrocarbonaceous material using a constructed infrastructure and associated systems maintained under positive pressure

A METHOD OF RECOVERING HYDROCARBONS FROM HYDROCARBONACEOUS MATERIALS CAN INCLUDE FORMING A CONSTRUCTED PERMEABILITY CONTROL INFRASTRUCTURE (100).THIS CONSTRUCTED INFRASTRUCTURE (100) DEFINES A SUBSTANTIALLY ENCAPSULATED VOLUME.A COMMINUTED HYDROCARBONACEOUS MATERIAL CAN BE INTRODUCED INTO THE CONTROL INFRASTRUCTURE TO FORM A PERMEABLE BODY (120) OF HYDROCARBONACEOUS MATERIAL.THE PERMEABLE BODY (120) CAN BE HEATED SUFFICIENT TO REMOVE HYDROCARBONS THEREFROM.DURING HEATING AND REMOVAL OF HYDROCARBONS AND SUBSEQUENT THERETO A POSITIVE PRESSURE CAN BE MAINTAINED WITHIN THE ENCAPSULATED. VOLUME BY MEANS OF A NONEOXIDIZING GAS TO EXPEDITE FLUSHING OF HYDROCARBONACEOUS MATERIAL, INHIBIT UNWANTED ENTRY OF OXYGEN INTO THE ENCAPSULATED VOLUME AND REMOVE RECOVERABLE HYDROCARBONS FOLLOWING THE HEATING PROCESS.

A thermal dismantling unit and a high temperature furnace

This invention is related to a thermal dismantling unit that; " Reaches high temperatures (up to 3500oC), " Has been designed to be able to work with the three states (solid, liquid and gas) of fuel, " Works at low pressure by using a special vacuum circuit, " Bears a washing system in order to produce clean hot air suitable for domestic and industrial usage.

Microwave reactor

The subject of the invention is a microwave reactor, which includes a source of microwave radiation, a reaction space with a hole for the cap of the reactor for the passage of microwave radiation into the reaction space, the main exhaust related to the reaction space for collecting burnt gases from the reaction space, to the cap hole of the reactor connected by its mouth consisting of a shell - the wave duct runs from the cap hole of the reactor to the micro wave radiation source and at the microwave radiation source it has the main partition wall to separate the under-pressure part of the microwave reactor from the microwave radiation source, located in the atmospheric pressure, where microwave radiation can pass through the main partition wall. The nature of the invention is based on the fact that the microwave reactor contains an additional exhaust to prevent the entry of burnt gas s into the wave duct in front of the main partition wall - this additional exhaust has the beginning terminated in the wave duct in its shell or into the cap of the hole of the reactor cap.

Methods of recovering hydrocarbons from hydrocarbonaceous material using a constructed infrastructure and associated systems maintained under positive pressure

A method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (100). This constructed infrastructure (100) defines a substantially encapsulated volume. A comminuted hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body (120) of hydrocarbonaceous material. The permeable body (120) can be heated sufficient to remove hydrocarbons therefrom. During heating and removal of hydrocarbons and subsequent thereto a positive pressure can be maintained within the encapsulated volume by means of a non-oxidizing gas to expedite flushing of hydrocarbonaceous material, inhibit unwanted entry of oxygen into the encapsulated volume and remove recoverable hydrocarbons following the heating process.

Pyrolysis installation

本发明公开了一种热解装置，包括：热解炉、冷却器组件和气体储罐，热解炉包括炉体、两个布料板和加热辐射管，炉体上设有油气出口，两个布料板在上下方向上间隔开地设在所述炉体内，每个布料板上设有在厚度方向上贯穿的多个通孔，加热辐射管设在炉体内且加热辐射管位于两个布料板之间。冷却器组件与油气出口相连。气体储罐与冷却器组件相连以接收热解气。根据本发明实施例的热解装置，加快了物料的升温且使得物料受热均匀，无结焦，有效增加单次处理量，可以充分利用加热辐射管的辐射热，提高了热解装置的热效率。从而便于油气混合物的释放，且使得产生的油气混合物中的固态产物少，避免了油气出口堵塞。

CONVECTION HEATING SYSTEMS FOR EXTRACTING HYDROCARBONS FROM ENCAPSULATED PERMEABILITY CONTROL INFRASTRUCTURES

Une infrastructure de contrôle de perméabilité construite (100) peut comprendre une retenue de contrôle de perméabilité qui définit un volume sensiblement encapsulé. L'infrastructure (100) peut également comprendre un matériau broyé hydrocarboné dans le volume encapsulé. Le matériau broyé hydrocarboné peut former un corps perméable (120) de matériau hydrocarboné. L'infrastructure (100) peut également comprendre au moins un conduit d'entraînement par convection orienté dans une partie inférieure du corps perméable (120) pour générer des réseaux d'écoulement par convection en masse à travers le corps perméable (120). Un procédé associé d'extraction d'hydrocarbures à partir de matériaux hydrocarbonés peut comprendre la formation d'une infrastructure de contrôle de perméabilité construite (100) qui définit un volume sensiblement encapsulé. Il est possible d'introduire un matériau hydrocarboné broyé dans l'infrastructure de contrôle (100) pour former un corps perméable (120) de matériau hydrocarboné. Il est possible de faire passer un fluide chauffé à travers le corps perméable (120) selon des réseaux de circulation par convection en masse pour extraire les hydrocarbures du corps perméable (120). Les hydrocarbures extraits peuvent être collectés pour utilisation et/ou traitement ultérieur. A constructed permeability control infrastructure (100) may include a permeability control retainer that defines a substantially encapsulated volume. The infrastructure (100) may also include a hydrocarbon milled material in the encapsulated volume. The hydrocarbon milled material can form a permeable body (120) of hydrocarbon material. The infrastructure (100) may also include at least one convective drive conduit oriented in a lower portion of the permeable body (120) for generating mass convective flow networks through the permeable body (120). An associated process for extracting hydrocarbons from hydrocarbon materials may include forming a ...

Waste material processing for oil recovery

An enhanced oil recovery method and apparatus for thermal processing of polymer-based waste to produce organic and inorganic processed materials. The organic and inorganic processed materials are injected as an injection stream into the ground to liberate ground oil. The liberated ground oil is withdrawn from the ground. The injection stream interacts with the ground oil to form a new oil and the new oil including the ground oil is withdrawn from the ground. Thermal processing is done with pyrolysis of waste tires.

Thermal-catalytic decomposition-pyrolysis device for organic waste

본 명세서는 유기 폐기물의 열-촉매 분해-열분해 장치에 관한 것으로, 장치는: 공급 라인에 의해 반응기에 연결된 저장소로서, 공급 라인에는 밸브가 배치되고, 반응기는, 반응기의 바닥으로부터 높이의 대략 1/3에 해당하는 최대 레벨에 위치한 가열 요소 및/또는 방사선원을 포함하는, 저장소; 및 반응기의 바닥으로부터 높이의 1/3에 해당하는 최대 레벨에 배치된 온도 센서를 포함하고, 출력 라인은 냉각기가 연결된 반응기의 뚜껑으로부터 돌출되고, 출력 라인의 단부는 생성물 가스를 배출하기 위한 분기를 통해 액화 생성물을 수용하기 위한 수용기의 오리피스에 연결된다.

Compound dry distiller used for manure processing

本发明公开了一种复式畜粪干馏器，所述干馏器包括高温炉，畜粪炭干馏箱，畜粪活性炭干馏箱；所述高温炉沿着水平方向分为第一端和第二端，所述高温炉的第一端底部设有燃料加热组件，第二端的顶部设有烟囱，且沿着所述高温炉的第一端至第二端的方向，所述高温炉依次分为第一温度段、第二温度段和第三温度段；沿着所述高温炉的水平方向，所述畜粪炭干馏箱的第一端位于所述第二温度段，第二端位于所述高温炉的第二端外等。本发明中这种装置的结构紧凑，使用方便安全，工艺易于控制，而且干馏处理粪便的有益效果显著。

A kind of external-heat continuous charcoal production system

本发明公开了一种外热式连续生物炭生产系统，包括碳化系统、加热系统、余热采收系统和裂解油气分离系统，其中，所述碳化系统由裂解腔、保温层、物料传输和搅拌组件、碳化热流通道组成，裂解腔呈圆柱形管状，物料传输和搅拌组件安装于裂解腔中，在裂解腔外部包裹有保温层，在裂解腔外壁与保温层之间设有所述碳化热流通道，碳化热流通道呈螺旋状环绕于裂解腔外壁，碳化热流通道的加热气流进口与加热系统连接，碳化热流通道的出气口与余热采收系统连接；裂解油气分离系统与裂解腔内连通。本发明能够准确地调控碳化所需要的最高温度，能够为裂解腔提供平稳的加热环境，并自后向前形成一个温度梯度，有助于定制生物炭的性质。

Method for preparing alcoholic liquor using Sasa quelpaertensis

본 발명은 조릿대숯 필터를 제조하는 단계로서, a) 야생 조릿대 줄기를 채취하고, b) 상기 조릿대 줄기에 열을 가하여 숯을 제조하고, c) 상기 숯을 원탄, 입상탄, 또는 분탄 형태의 조릿대숯 필터를 제조하는 단계; 주류 제조용 주조용수를 상기 조릿대숯 필터로 여과하는 단계; 주류 제조용 주류 원액을 상기 조릿대숯 필터로 여과하는 단계; 및 상기 주조용수와 주류 원액을 혼합하는 단계를 포함하며, 상기 조릿대 줄기는 연소통에 장입하고 연소통 내부 온도를 300 ~ 500℃으로 유지하여 5시간 ~ 10시간의 범위로 가열하여 숯으로 제조하는 것을 특징으로 하는 조릿대숯을 이용한 주류 제조방법을 제공한다. A method for producing a saddle charcoal filter, comprising the steps of: a) collecting a stem of a wild type bark, b) applying heat to the saddle stalk to produce char, c) Producing a char filter; Filtering the main preparation water for mainstream production with the saddle charcoal filter; Filtering the main stock solution for mainstream production with the saddle charcoal filter; And mixing the main tank water and a stock solution, wherein the sausage stem is charged into a sintering cylinder and heated to a temperature ranging from 5 to 10 hours by maintaining the internal temperature of the sintering cylinder at 300 to 500 ° C to produce charcoal The present invention also provides a method for producing a liquor using sour charcoal.

Apparatus and method for making fuel using forest residue

An apparatus and a method for generating fuel form forest residue are provided to facilitate conveying, storing, and burning of biomass and increase the amount of heat generated through burning of the biomass. Fuel is generated in a palletizer(35) by sending various kinds of forest residue from a first input unit(10) to a pulverization unit(12), pulverizing the forest residue to generate a first raw material in the pulverization unit, and performing middle processes on the first material. A second input unit(20) is simultaneously connected to a downstream side of the first input unit and a mixer(15). The second input unit contains a second raw material, which is mixed into the first raw material. A carbonizer(22) is installed at a downstream side of the mixer to receive a middle raw material. The carbonizer carbonizes the middle raw material at a high speed under a high temperature. A pulverizer(26) is installed at a downstream side of the carbonizer to receive the carbonized raw material. The pulverizer pulverizes the middle raw material, which is cooled through a cooler(24), into fine particles. A third input unit(30) is simultaneously connected to a downstream side of the pulverizer and the mixer. The third input unit receives a third raw material, which is mixed to the pulverized middle raw material particles. Further, the carbonizer controls an air-supporting part(16) and a gas-supporting part(18) in order to maintain a temperature ranged from 400 to 700 ‹C.

Pyrolysis method for heating medical waste or waste plastic by molten salt

一种熔融盐加热医疗废弃物或废旧塑料的热解方法，包括如下步骤：(1)熔融盐预处理，(2)医疗废弃物或废旧塑料预处理，(3)将步骤(1)熔融盐预处理得到的熔融盐混合固体颗粒放入熔融盐储存罐；(4)将步骤(2)得到的医疗废弃物或废旧塑料固体颗粒或聚氯乙烯固体颗粒放入料仓中；将高温熔融盐放至热解炉，同时将料仓中的医疗废弃物颗粒或聚氯乙烯颗粒下放至热解炉中进行热解，获得高品质的液体油，采用本发明能够实现医疗废弃塑料的有效利用，减少医疗废弃塑料清洁处理与管道维护所需的成本并减少二次污染，在医疗废弃物综合利用和可再生能源技术领域有广阔的应用前景。

Apparatus and method for making fuel using forest residue

Disclosed herein is an apparatus for producing fuel from forest residues, in which a variety of forest residues are sent from a first feeder (10) to a crusher (10), in which they are crushed, and the crushed material is subjected to intermediate processes and produced as standardized fuel in a pelletizer (35). The apparatus comprises: a second feeder (20), connected with both the downstream of the first feeder (10) and a mixer (15) and adapted to receive a second raw material for mixing with the first crushed raw material; a carbonizer (22) disposed downstream of the mixer (15) so as to receive an intermediate raw material and adapted to carbonize the intermediate raw material at high temperature and high speed; a crusher (26) disposed downstream of the carbonizer (22) so as to receive the carbonized intermediate material and adapted to crush the intermediate raw material, cooled in a cooler (24), into fine particles; and a third feeder (30) connected with both the downstream of the crusher (26) and a mixer (32) and adapted to receive a third raw material for mixing with the finely crushed intermediate raw material. Accordingly, the apparatus makes it convenient to transport, store and burn the biomass and can increase the heating value of combustion of the biomass, such that the biomass can provide an economic energy source.

A kind of damaged tire cracking black carbon carbonization system

本发明公开了一种废轮胎裂解炭黑碳化系统，其连续式热裂解炉采用连续式回转热裂解炉，可实现废轮胎连续进出料裂解工作；高效微波碳化装置通过高温使炭黑实现碳化，增加炭黑的深加工性能；炭黑冷却装置将碳化后的炭黑进行降温冷却，防止炭黑高温自燃，方便后期储存输送；炭黑料仓可以暂存一定炭黑，防止其他配合装置故障导致系统停歇，从而保证整套裂解系统的连续性。本发明对裂解炭黑的碳化，大大提高了炭黑的深加工性能，有较好的生产连续性和密封性，炭黑碳化过程高效快速，冷却时间短；整个装置密封工作，安全环保，全自动化进出料，操作简单方便。

Data output buffer whose mode switches according to operation frequency and semiconductor memory device having the same

A data output buffer switches it operating mode according to its operating frequency. The data output buffer includes a delay control unit, and a buffer unit. The buffer unit provides data of an internal buffer input line to an external buffer output line. The delay control unit generates a buffer enable signal corresponding to a received reference control signal. The buffer unit blocks the provision of the data to the buffer output line in response to a deactivation of the buffer enable signal. The buffer enable signal remains in an activated state when the period of the reference control signal is shorter than a reference period. The data output buffer may be included in a semiconductor memory device.

System and method for recycling waste into energy

A system for recycling solid waste into energy includes a heated enclosure 66 , one or more input conveyors 60, 67 move waste materials through the heated enclosure, provide a flow line with a temperature gradient of at least 150F°, and mechanically move the waste particles and the residual solids along the flow line. A heated rotary drum 74 is in fluid communication with the flow line, and condenser unit 94, 98 receive vapors from the flow line and the rotary drum and output hydrocarbons. One or more discharge conveyors 76 discharge carbon black from the rotary drum. Control valves 80, 82 seal a vacuum downstream from the discharge conveyors, and control valves 34, 46 seal vacuum upstream from the one or more input conveyors. Various types of vacuum pumps may be used to maintain a selected vacuum between the control valves.

Control system to regulate indirect heating system used in association with incineration of pyrolysis gases arising from charcoal production

A charcoal kiln assembly has an indirectly regulated heating system in which the pyrolysis gases are burned. The gas passages incorporate blowers and pressure detectors (F1-F13). Gas combustion is regulated using pressure information derived from the burner chamber, pyrolysis and smoke gas passages.

Method for preparing biochar and hydrogen by utilizing anaerobic fermentation byproducts

A method for preparing biochar and hydrogen by utilizing anaerobic fermentation byproducts, the method including: (1) mixing a first straw, seeding sludge and distilled water, and then carrying out anaerobic fermentation to obtain a mixed product after fermentation; (2) performing separation on the mixed product to obtain a second straw and biogas slurry; and (3) carbonizing the second straw to obtain biochar, and collecting gas after a pressurized catalytic reaction on the biogas slurry to obtain hydrogen.

生物质催化转化制备生物质炭的装置

本发明公开了一种生物质催化转化制备生物质炭的装置，生物质催化转化制备生物质炭的装置包括外炉组件、设于外炉组件内的内炉组件、蒸汽组件和催化剂组件，外炉组件炉体内部形成有容纳腔，外炉组件上设置有进汽管道和催化剂管道，蒸汽组件与进汽管道的一端连通，催化剂组件与催化剂管道的一端连通。内炉组件可移动设置于容纳腔内，该内炉组件包括：物料仓、加热管组和催化剂管组，加热管组和催化剂管组间隔设置于物料仓内，加热管组与进汽管道的另一端连通，将催化剂管组与催化剂管道连接。由此，通过将内炉组件设置于封闭的外炉组件内可以起到制炭和取炭的操作分离，提升制炭效率，同时也能实现安全高效制炭。

一种微波热解系统及其使用方法

本发明公开了一种微波热解系统及其使用方法，本发明在微波热解段、活性炭段和石墨段上均设置有微波发生器，在微波热解段内从下至上依次设置有挡板和防尘罩，粉煤在微波热解段热解，同时产生了荒煤气和少量的粉尘，荒煤气携带粉尘上升，经过设置在微波热解段内的多层挡板时，大量的粉尘被挡住并在重力的作用下下沉，少量的粉尘继续被荒煤气携带上升至防尘罩，粉尘进一步被隔离，通过微波发生器加热，微波热解具有独特的热传导规律、整体内外加热均匀、升温速率快、选择加热的特点，可对煤炭、油泥和油页岩材料进行热解，提高热解效率，增加热解产物收率和提升产品质量，得到的荒煤气氮气含量得到了控制，可得到高质量的荒煤气。

炭化油化処理炉

【課題】比較的安価に製作でき、かつ稼働に伴う腐食による劣化が少なく、さらに低コストで維持管理することができる炭化油化処理炉を提供する。【解決手段】この炭化油化処理炉１Ａは、外部から供給される過熱水蒸気によりプラスチックごみを含む廃棄物を炭化処理および油化処理するように構成されており、炭化油化処理炉１Ａは、鉄製の外側構造体４，６と、この外側構造体４，６に対して分離可能なステンレス製の内側構造体５，７とで構成されている。【選択図】図１

炭化油化処理炉

【課題】比較的安価に製作でき、かつ稼働に伴う腐食による劣化が少なく、さらに低コストで維持管理することができる炭化油化処理炉を提供する。【解決手段】この炭化油化処理炉１Ａは、外部から供給される過熱水蒸気によりプラスチックごみを含む廃棄物を炭化処理および油化処理するように構成されており、炭化油化処理炉１Ａは、鉄製の外側構造体４，６と、この外側構造体４，６に対して分離可能なステンレス製の内側構造体５，７とで構成されている。【選択図】図１

炭化油化処理炉

一种太阳能聚热的生物炭制备装置

本发明提供一种太阳能聚热的生物炭制备装置，涉及生物炭制备装置领域；太阳能聚热的生物炭制备装置包括：箱体、箱盖、聚热组件、导热组件和通风管；箱盖与箱体转动连接，用于封闭或者打开箱体的顶部；箱盖为中空双层结构，箱盖的上层板上设置透光孔；聚热组件设置在箱盖的上层板上，用于将太阳光通过透光孔聚焦至导热组件的上端；导热组件贯穿设置在箱盖的下层板上，用于将导热组件上端的热能导入至箱体的内部；通风管贯穿设置在箱盖上；通风管上位于箱体内的一端设置有单向阀，用于将箱体内的气体排出至外部；本发明能够利用太阳能制备生物炭，结构简单，且能避免因使用火力或者电力烧制生物炭导致的能源浪费。

Intermediate vapor collection within encapsulated control infrastructures

A method of recovering hydrocarbons from hydrocarbonaceous materials can include forming a constructed permeability control infrastructure (600). This constructed infrastructure (600) defines a substantially encapsulated volume. A mined hydrocarbonaceous material can be introduced into the control infrastructure to form a permeable body (605) of hydrocarbonaceous material. The permeable body (605) can be heated sufficient to remove hydrocarbons therefrom. Hydrocarbon products can be collected from intermediate locations (620, 630) within the permeable body (605). Advantageously, an intermediate fluid collection system (610) can be used to draw a hydrocarbon product from the permeable body (605) at preselected locations. Such intermediate collection can provide hydrocarbon product fractions which can reduce or eliminate the need for full-scale distillation of a hydrocarbon product having a full range of products such as that typically found in crude oil. In addition, product quality can be tailored by monitoring such intermediate draws and adjusting operating parameters accordingly.

一种海洋藻类生物质炼制装置

本发明公开了一种海洋藻类生物质炼制装置，属于生物能源设备技术领域，其包括釜体和转动加热机构，转动加热机构包括：加热管，每根加热管的外侧套装有碳化硅保护管；保护管安装板；法兰盘，保护管安装板固定在法兰盘的底部，法兰盘通过转动密封机构与釜体的上端口连接；驱动机构，驱动机构用于驱动法兰盘转动；配电盒，加热管穿过法兰盘后与配电盒连接。本发明提供的海洋藻类生物质炼制装置，使加热管和釜内藻类生物质隔离，避免加热管表面粘附物料。碳化硅保护管能够抵抗高温变形，因此内置加热管的碳化硅保护管在高温状态下能够保持优异的强度并随着法兰盘转动，达到边加热边搅拌釜体内藻类生物质的目的，有效利用装置内部空间。

바이오매스 반탄화 장치

본 발명은, 바이오매스 반탄화 장치에 관한 것으로서, 내부에 형성된 반탄화실을 구비하는 본체; 상기 반탄화실에 설치되며, 내부에 바이오매스 원료가 수용되는 석영관; 및 상기 석영관을 향해 마이크로웨이브를 발진하여, 상기 석영관을 투과한 상기 마이크로웨이브를 이용해 상기 바이오매스 원료를 반탄화하는 마그네트론을 포함한다.

Pyrolysis reactor system for the conversion and analysis of organic solid waste

The pyrolysis reactor system for the conversion and analysis of organic solid waste is a dual gas-liquid separation system, allowing for the conversion of organic solid waste, as well as analysis of the conversion products. A pyrolysis reactor is provided for converting the organic solid waste into a solid product and a gas-liquid product mixture through pyrolysis. A source of carrier gas is in fluid communication with the pyrolysis reactor for degrading the organic solid waste. A first gas-liquid separator is in fluid communication with the pyrolysis reactor and receives the gas-liquid product mixture therefrom, separating a portion of gas therefrom. A second gas-liquid separator is in fluid communication with the first gas-liquid separator and receives the gas-liquid product mixture therefrom and separates the remainder of the gas therefrom. The remainder of the gas and the separated liquid are each collected separately from one another, in addition to the char.

Termokatalitikus bontásra szolgáló készülék - szerves hulladékanyagok pirolízise

Sposób pirolizy (rozkładu termicznego) stałych odpadów organicznych oraz reaktor do przeprowadzania tego sposobu

Device for thermal-catalytic decomposition-pyrolysis of organic waste materials

The specification relates to the device for thermal-catalytic decomposition—pyrolysis of waste organic materials, comprising: the reservoir, linked by means of the supply line with the reactor, where in the line is arranged the valve, wherein the reactor contains the heating element and/or the radiation source situated approximately up to the maximum level corresponding to ⅓ of the height from the bottom of the reactor; and the temperature sensor placed up to the maximum level corresponding to ⅓ of the height from the bottom of the reactor, wherein the output line protrudes from the lid of the reactor with the linked cooler, wherein the end of the output line is connected to the orifice on the receiver to contain liquefied products via the branch to exhaust product gases.

一种生物炭生产装置及其冷却系统

本发明公开了一种生物炭生产装置及其冷却系统，包括燃烧室、反应釜、烟槽、封盖、冷却仓、冷却管、喷淋管、橡胶管和环管，所述燃烧室内部设置有反应釜，所述反应釜上端设置有封盖，所述反应釜上端边缘与燃烧室上端之间设置有烟槽，所述封盖上端安装有电机，且电机下端设置有贯穿封盖的传动轴，所述传动轴表面设置有呈螺旋状分布的绞片，所述烟槽内部设置有烟气管，所述反应釜与封盖之间设置有橡胶管；所述封盖上端一侧连接有输气管，所述燃烧室一侧设置有冷却仓，所述输气管一端与冷却仓内部底端相连通。本发明不仅可实现生物炭原料的输送和排出，还能在加热过程中进行搅拌作业，并且还具备更好的烟气回收以及气体冷却效果。

一种利用磁场调控生物质热解产物特性的系统和方法

本发明公开了一种利用磁场调控生物质热解产物特性的系统方法，系统包括热解炉炉体，热解炉炉体外周设置有活动保温墙，热解炉炉体顶部设置有出口分别与氮气瓶和冷凝器相通，其特征在于，所述热解炉炉体底部设置具有耐高温特性的永久磁铁，使炉内有磁场分布。本发明以磁场代替催化剂达到生物质热解油粘度降低目的，避免了生物炭受催化剂污染，从而实现了热解后生物炭回收利用。所需热解温度降低，减少了催化剂所需成本，实现了生物油源头降粘，省略了生物油后期提质降粘处理工艺，该降粘方式绿色、经济，不需使用催化剂就能达到生物油品质提高效果，是制备高品质生物油的重要手段，对生物质液体燃料制备具有重要意义。

폐기물의 열분해／가스화법을 이용한 연료전지 열병합 발전 시스템

본 발명은 폐기물의 열분해/가스화법을 적용한 연료전지 열병합 발전 시스템에 관한 것으로, 보다 상세하게는 가연성 폐기물에 열분해/가스화 공정을 적용하여 H 2 , CO를 비롯하여 CH 4 , CO 2 , H 2 O, H 2 S, HCl, N 2 등 다양한 열분해 가스를 생산한 후, 상기 열분해 가스를 용융탄산염형 연료전지(MCFC) 또는 고체산화물 연료전지(SOFC) 등에 공급하여 연료로 사용할 수 있는 연료전지 열병합 발전 시스템에 관한 것이다. 본 발명은 가연성 폐기물의 열분해 공정을 통하여 얻어지는 열분해 가스를 증기 또는 가스터빈 발전이 아닌 연료전지에 연료가스로서 이용함으로써 높은 발전효율은 물론 열에너지도 효과적으로 이용할 수 있는, 고효율이면서도 친환경적인 연료전지 열병합 발전 시스템을 제공할 수 있다. 연료전지 열병합 발전 시스템, 연료전지, 용융탄산염형 연료전지, 고체산화물 연료전지, 가연성 폐기물, 열분해, 가스화, 열분해 가스, 열병합, 고 발전효율

可调式一体炉

本发明公开了一种可调式一体炉。可调式一体炉包括炉体和可调式支撑机构，可调式支撑机构包括炉体和可调式支撑机构，可调式支撑机构包括支撑升降器、连杆、导向杆、第一温度传感器和支撑体，支撑升降器安装在炉体的顶部，炉体具有内腔，内腔包括进料段和预热段，升降器与连杆固定，导向杆固定在进料段内，连杆穿设在导向杆内，连杆的下端与支撑体固定，第一温度传感器设在预热段内，第一温度传感器至少两个，第一温度传感器设用于检测支撑体所在位置的温度，当支撑体所在位置的温度超过预定温度时，支撑升降器带动连杆上升，连杆带动支撑体上升。本发明可调式一体炉能够避免预热段的型煤破裂、变形或结块。

生物质催化转化制备生物质炭的装置

本发明公开了一种生物质催化转化制备生物质炭的装置，生物质催化转化制备生物质炭的装置包括外炉组件、设于外炉组件内的内炉组件、蒸汽组件和催化剂组件，外炉组件炉体内部形成有容纳腔，外炉组件上设置有进汽管道和催化剂管道，蒸汽组件与进汽管道的一端连通，催化剂组件与催化剂管道的一端连通。内炉组件可移动设置于容纳腔内，该内炉组件包括：物料仓、加热管组和催化剂管组，加热管组和催化剂管组间隔设置于物料仓内，加热管组与进汽管道的另一端连通，将催化剂管组与催化剂管道连接。由此，通过将内炉组件设置于封闭的外炉组件内可以起到制炭和取炭的操作分离，提升制炭效率，同时也能实现安全高效制炭。

一种利用固定床褐煤干燥器干馏褐煤工艺及系统

一种利用固定床褐煤干燥器干馏褐煤工艺及系统，将褐煤装入固定床褐煤干燥器内，通入温度介于105℃-260℃的低温工作介质至固定床褐煤干燥器的间壁换热器内，干燥褐煤至达到下一工艺要求，更换或加热介质，通入温度介于400℃-1000℃的高温工作介质至固定床褐煤干燥器的间壁换热器内，干馏褐煤至达到工艺要求，然后卸出热褐煤，以及组成实现利用固定床褐煤干燥器干馏褐煤工艺的系统，在本发明中，固定床褐煤干燥器没有任何运转部件，在一个床体上完成干燥和干馏过程，大大的简化了操作，满足褐煤干馏的特殊性要求，提高褐煤的干馏产品质量，并且，褐煤在深度干燥后的全水很低，对干馏气的洁净高效分离有利，提高焦油收油率，提高褐煤干馏的经济性。

一种带有干熄装置的电加热干馏炉

本发明涉及一种带有干熄装置的电加热干馏炉，包括电加热干馏炉，所述电加热干馏炉是由多个干馏炉并排组成的炉组；每个干馏炉均从上到下依次设置有炉顶区、存料区、干馏区、冷却区及落料区；炉顶区设装煤装置及煤气导出装置；干馏区包括多个干馏室，每个干馏室的侧壁内均设有测温装置及电加热装置；冷却区包括多个冷却室，每个冷却室内设有多个低温载气通道。本发明采用间接电加热，结合测温装置和低温载气冷却装置耦合控制，实现低阶煤干馏加热的精准控制，提高了干馏固体产品的质量；干馏炉下部设置干熄装置对干馏固体进行热量回收，干熄装置采用低温载气作为冷源，有利于降低装置的整体功耗。

生物质炭化炉

本发明公开了一种生物质炭化炉，生物质炭化炉包括炉壳、蒸汽组件、催化剂组件和辅助件，其中，炉壳竖向设置，炉壳内部形成有物料仓，蒸汽组件设于炉壳上，以用于加热物料仓内的物料，催化剂组件设于炉壳上且与蒸汽组件竖向间隔分布，以用于释放催化剂至物料仓内，辅助件可移动地插设于物料仓内，由此，通过设置辅助件可以预留出生物质炭的分离空间，从而有利于生物质炭的取炭操作，促进生物质炭的下落，提高炭化炉的取炭效率。

生物质炭化炉

本发明公开了一种生物质炭化炉，生物质炭化炉包括炉壳、蒸汽组件、催化剂组件和辅助件，其中，炉壳竖向设置，炉壳内部形成有物料仓，蒸汽组件设于炉壳上，以用于加热物料仓内的物料，催化剂组件设于炉壳上且与蒸汽组件竖向间隔分布，以用于释放催化剂至物料仓内，辅助件可移动地插设于物料仓内，由此，通过设置辅助件可以预留出生物质炭的分离空间，从而有利于生物质炭的取炭操作，促进生物质炭的下落，提高炭化炉的取炭效率。

Verfahren und Vorrichtung zum Herstellen von Koks

一种利用固定床褐煤干燥器干馏褐煤工艺及系统

一种利用固定床褐煤干燥器干馏褐煤工艺及系统，将褐煤装入固定床褐煤干燥器内，通入温度介于105℃-260℃的低温工作介质至固定床褐煤干燥器的间壁换热器内，干燥褐煤至达到下一工艺要求，更换或加热介质，通入温度介于400℃-1000℃的高温工作介质至固定床褐煤干燥器的间壁换热器内，干馏褐煤至达到工艺要求，然后卸出热褐煤，以及组成实现利用固定床褐煤干燥器干馏褐煤工艺的系统，在本发明中，固定床褐煤干燥器没有任何运转部件，在一个床体上完成干燥和干馏过程，大大的简化了操作，满足褐煤干馏的特殊性要求，提高褐煤的干馏产品质量，并且，褐煤在深度干燥后的全水很低，对干馏气的洁净高效分离有利，提高焦油收油率，提高褐煤干馏的经济性。

Intermediate vapor collection within encapsulated control infrastructures