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RU2004113074A - METHOD FOR CONTINUOUS THERMOCHEMICAL PROCESSING OF CARBON-CONTAINING RAW MATERIALS - Google Patents

METHOD FOR CONTINUOUS THERMOCHEMICAL PROCESSING OF CARBON-CONTAINING RAW MATERIALS Download PDF

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Publication number
RU2004113074A
RU2004113074A RU2004113074/15A RU2004113074A RU2004113074A RU 2004113074 A RU2004113074 A RU 2004113074A RU 2004113074/15 A RU2004113074/15 A RU 2004113074/15A RU 2004113074 A RU2004113074 A RU 2004113074A RU 2004113074 A RU2004113074 A RU 2004113074A
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RU
Russia
Prior art keywords
raw materials
carbon
containing raw
reducing gas
reactor
Prior art date
Application number
RU2004113074/15A
Other languages
Russian (ru)
Other versions
RU2292299C2 (en
Inventor
Сергей Петрович Хмеленко (RU)
Сергей Петрович Хмеленко
Original Assignee
Сергей Петрович Хмеленко (RU)
Сергей Петрович Хмеленко
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Сергей Петрович Хмеленко (RU), Сергей Петрович Хмеленко filed Critical Сергей Петрович Хмеленко (RU)
Priority to RU2004113074/15A priority Critical patent/RU2292299C2/en
Publication of RU2004113074A publication Critical patent/RU2004113074A/en
Application granted granted Critical
Publication of RU2292299C2 publication Critical patent/RU2292299C2/en

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Classifications

    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Carbon And Carbon Compounds (AREA)

Claims (3)

1. Способ непрерывной термохимической переработки углеродсодержащего сырья, включающий переработку различных видов углеродсодержащего сырья при 200-950°С в среде восстановительного газа с подачей пара, дальнейшее охлаждение и выгрузку активированного угля, причем восстановительный газ получают сжиганием углеводородного топлива с коэффициентом расхода воздуха менее 1,0 и смешивают его с газами процесса термохимической обработки, отличающийся тем, что восстановительный газ смешивают с газами процесса термохимической обработки в соотношении 1:(0,1-10), подают не менее чем в три зоны реактора, причем смешение происходит перед подачей в каждую реакторную зону в той пропорции, которая обеспечивает необходимый температурный режим и соответствует условиям производства продукта с заданными параметрами.1. A method for the continuous thermochemical processing of carbon-containing raw materials, comprising processing various types of carbon-containing raw materials at 200-950 ° C in a reducing gas medium with steam supply, further cooling and unloading of activated carbon, wherein the reducing gas is obtained by burning hydrocarbon fuel with an air flow coefficient of less than 1, 0 and mix it with the gases of the thermochemical treatment process, characterized in that the reducing gas is mixed with the gases of the thermochemical treatment process in the ratio 1: (0.1-10), is fed to at least three zones of the reactor, and mixing occurs before feeding into each reactor zone in the proportion that provides the necessary temperature and meets the conditions for the production of the product with the specified parameters. 2. Способ по п.1, отличающийся тем, что насыщенный водяной пар температурой 110-120° подается в нижнюю часть реактора дозировано в массовом соотношении к получаемому углю как (0,05-10):1, в зависимости от свойств сырья и заданных параметров продукта.2. The method according to claim 1, characterized in that the saturated water vapor with a temperature of 110-120 ° is supplied to the lower part of the reactor in a proportioned weight ratio to the obtained coal as (0.05-10): 1, depending on the properties of the raw materials and the specified product parameters. 3. Способ по п.1, отличающийся тем, что газообразный теплоноситель после термической подготовки сырья и/или сушки частично возвращается и смешивается с поступающим теплоносителем в соотношении (4-20):1.3. The method according to claim 1, characterized in that the gaseous coolant after thermal preparation of the raw materials and / or drying is partially returned and mixed with the incoming coolant in the ratio (4-20): 1.
RU2004113074/15A 2004-04-28 2004-04-28 Method of continuously thermochemically processing hydrocarbon stock RU2292299C2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
RU2004113074/15A RU2292299C2 (en) 2004-04-28 2004-04-28 Method of continuously thermochemically processing hydrocarbon stock

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
RU2004113074/15A RU2292299C2 (en) 2004-04-28 2004-04-28 Method of continuously thermochemically processing hydrocarbon stock

Publications (2)

Publication Number Publication Date
RU2004113074A true RU2004113074A (en) 2005-10-10
RU2292299C2 RU2292299C2 (en) 2007-01-27

Family

ID=35851018

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2004113074/15A RU2292299C2 (en) 2004-04-28 2004-04-28 Method of continuously thermochemically processing hydrocarbon stock

Country Status (1)

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RU (1) RU2292299C2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2356932C1 (en) * 2007-09-28 2009-05-27 Закрытое акционерное общество "Лонас технология" Furnace for activation of charcoal
RU2378319C1 (en) * 2008-08-01 2010-01-10 Учреждение Российской Академии Наук Объединенный Институт Высоких Температур Ран (Оивт Ран) Method of obtaining hydrocarbon fuel and hydrocarbon materials from biomass
RU2481386C2 (en) * 2008-10-08 2013-05-10 Сергей Петрович Хмеленко Method for continuous thermochemical treatment of different types of carbon-containing material

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3876505A (en) * 1972-12-08 1975-04-08 Calgon Corp Manufacture of activated carbon from sized coal
DE3141906A1 (en) * 1981-10-08 1983-04-21 Degussa Ag, 6000 Frankfurt METHOD AND DEVICE FOR CARRYING OUT GAS / SOLID REACTIONS, IN PARTICULAR FOR ACTIVATING AND REACTIVATING ACTIVE CARBON
RU2023661C1 (en) * 1993-07-27 1994-11-30 Дзержинское производственное объединение "Заря" Method of activated carbon producing
RU2177977C2 (en) * 2000-01-12 2002-01-10 Антоненко Владимир Федорович Method for thermally processing biomass
RU2209179C2 (en) * 2001-08-30 2003-07-27 Закрытое акционерное общество "Научно-исследовательский институт ВНИИДРЕВ" Method of continuous thermochemical processing of carbon-containing raw materials and plant for method embodiment

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Publication number Publication date
RU2292299C2 (en) 2007-01-27

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Legal Events

Date Code Title Description
MM4A The patent is invalid due to non-payment of fees

Effective date: 20090429

NF4A Reinstatement of patent

Effective date: 20120220

MM4A The patent is invalid due to non-payment of fees

Effective date: 20160429