WO1999051709A1 - Combustible moule, variantes, et procedes de production de combustible moule - Google Patents

Combustible moule, variantes, et procedes de production de combustible moule Download PDF

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Publication number
WO1999051709A1
WO1999051709A1 PCT/RU1998/000219 RU9800219W WO9951709A1 WO 1999051709 A1 WO1999051709 A1 WO 1999051709A1 RU 9800219 W RU9800219 W RU 9800219W WO 9951709 A1 WO9951709 A1 WO 9951709A1
Authority
WO
WIPO (PCT)
Prior art keywords
mixture
fuel
sludge
binder
moulded
Prior art date
Application number
PCT/RU1998/000219
Other languages
English (en)
French (fr)
Russian (ru)
Inventor
Valery Grigorievich Lury
Original Assignee
Valery Grigorievich Lury
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
Priority claimed from RU98106931A external-priority patent/RU2130047C1/ru
Priority claimed from RU98111426/04A external-priority patent/RU2131449C1/ru
Application filed by Valery Grigorievich Lury filed Critical Valery Grigorievich Lury
Priority to EA199900319A priority Critical patent/EA000979B1/ru
Publication of WO1999051709A1 publication Critical patent/WO1999051709A1/ru

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L5/00Solid fuels
    • C10L5/40Solid fuels essentially based on materials of non-mineral origin
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • Non-sludge containing 10-20% of water, 2-10% of clay, sand and td, and 60- 90% of non-processed
  • technical carbon content of 10-20 and wood-based products (saws) - other a mixture of components absorbs at a pressure of 0.2 ° C and 20 ° C; They receive barriers with a compliant supply of 4760-6286 kcal / kg and a yield of 4.4- 3.4% ( ⁇ , 2010842? ⁇ 10 ⁇ 5 / 48, 04/15/94).
  • Briquettes of this composition are obtained by mixing the indicated ingredients, followed by the preparation of briquettes and drying (US, 2100415, 5 S105 / 44 27/12/97). Received briquettes have the following characteristics: density 0.52-0.68 g / cm; The air resistance is 13-16.7, the free range is 4100-4150 kcal / kg, the accuracy is at a bend of 0.8-1 ⁇ Pa, the residual humidity is 19-20%. _ _
  • the fuel obtained is obtained by mixing industrial silt with 40-50% by weight of coal dust or wood, or 24/8, 05/08, 05/08, 05/18, or 10, 8/8, or 5/8, or 8, 8/8, or 05, 46, 08, 5/8, or.
  • the posed problem is solved by a large number of inventions related to the general public, so that they will form a unified inventive concept.
  • the equipment is complied with, as it is claimed that it is fuels and the method of its receipt (that is, it is intended to be obtained from others), but also One-way products, one-time use, one-time and one-way treatment results.
  • FUEL-BASED FUEL ON BASED DRIED MIXTURES inclusive in% of the mass of the batch mix: lignosulphonate or molasses 2-7, and / or dehydrated activated sludge 3-8, and / or clay 3-10, and / or steam, or the next pump, 1 -6 - None, in wt.% ⁇ binder 10-32 and chopped solid fuel from the group: wood sawdust, wood, fossil fuels, charcoal sludge, lignin, non-liquefied mixed fuels
  • ⁇ ⁇ PL ⁇ ( ⁇ ) on the basis of a dried mixture of crushed solid fuel and condensed sludge from the unit
  • Estimated stocks of water account for 13-38 wt.% of condensed sludge with a water content of 5-14) and chopped solid fuels: wood (chopped, chopped) zh ⁇ m ⁇ neshyud ⁇ v, and ⁇ l ⁇ d ⁇ v ⁇ as ⁇ eny, ⁇ s ⁇ ch ⁇ i ⁇ l ⁇ d ⁇ v, d ⁇ blenye s ⁇ ebli ⁇ as ⁇ eny, d ⁇ blenye ⁇ dy ⁇ ⁇ bdi ⁇ a ⁇ u ⁇ u ⁇ uzny ⁇ ⁇ - cha ⁇ v, ⁇ isa, g ⁇ ech ⁇ i, semeche ⁇ , ⁇ shena, and g ⁇ chitsy d ⁇ ugi ⁇ ⁇ as ⁇ eny) ⁇ dy, ⁇ , lignin, or ⁇ s ⁇ vaya ug ⁇
  • the bulk of the sludge in the main part of the materials of the Ecuadorsian industry is up to 50 o, the fat is up to 30%> and the carbohydrate is up to 20%>; the activity of condensed sludge is sold as it is necessary to keep the adhesion properties dry, because of the drying of sludge when it is dried
  • the product is free from waste and has a good working temperature of 20 C - 0.85 - 0.99 ⁇ / m, the weight is between 2.5 and 60%; a flash transmitter in the crucible of a crucible of 145-250 C; The temperature of stagnation is 6–25 ° ⁇ , the content of the sulfur is 0.5–12%.
  • Fatty substances are used, for example, in case of raw oil, also called fusa, sunflower oil, pure oil and other oils. Fatty substances contain up to 60%> mechanical impurities in the form of particles of processed plants, mineral dust, up to 70% of fat, up to 40% of water and has a density of 0.8-1, 2 ⁇ / m 3 , a melting point of 10-80 ° ⁇ .
  • the boiler is 1/3 of the length of the mixer, away from the fuel loading area and part of the processed oil.
  • the mixture for sprinkling has the following proportions of components, in wt.%: Industrial engine oil -4 molasses -4 steam grinder -2 grilled -20 gr
  • Forms have a cylinder shape with a diameter of 50 mm and a length of 60-100 mm, the typical value for compression was 9.8 times, and the discharge was (after 4 times for the masses remained on the system, which indicates a good mechanical and the possibility of operating free-of-charge business facilities.
  • the briquettes had a ready-to-eat range of 5000-5200 kcal / kg, a density of 1, 08-1, 18 t / m, a moisture content of 12%> and contained a dried mixture in the following medium.
  • the briquettes had a density of 1, 07- 1, 19 ⁇ / m 1 , a reliable capacity of 4600-5050 kcal / kg, a moisture content of 5–9%, and an aggregate density of 95–11% of the total 96%> leftover on the system, which indicates a good mechanical impairment.
  • Briquettes have a tightness of 1, 1 - 1, 25 ⁇ / m '1 , tactile equipment 5500-5800 kcal / kg, humidity 5-7%, mechanical value 10.2-11.4
  • Is ⁇ lzuyu ⁇ ⁇ m ⁇ nen ⁇ y following: ⁇ s ⁇ vuyu mel ⁇ ch with si ⁇ vym s ⁇ s ⁇ av ⁇ m 0-6 mm z ⁇ ln ⁇ s ⁇ yu 1 1% vlazhn ⁇ - s ⁇ yu 8%, ⁇ ⁇ ⁇ ime ⁇ u ⁇ ° 1 ⁇ ab ⁇ ann ⁇ e mashinn ⁇ e masl ⁇ ⁇ ⁇ ime ⁇ u ⁇ ° 1 lign ⁇ sul ⁇ na ⁇ ⁇ ⁇ ime ⁇ u ⁇ > 2 ⁇ m ⁇ nen ⁇ y d ⁇ zi ⁇ uyu ⁇ and it is mixed in the following situation, in wt.%>: industrial engine oil -5 lignite -7 sulphate -10 quick-change -78 when the fuse is mixed, It is dried at a temperature of 295 ° C for 25 minutes before the rest ⁇
  • coal slurry made of coal of the grade ' ⁇ "with a sieve system of 0-1 mm, a grit of 1 1 -12%> and a moisture content of 10%, an industrial oil of 1 gallon / m 3 and clay with a moisture content of 18%>, the components take and mix for the following condition, in wt.%>:
  • Received products contain components in the following state, in wt.%>: Industrial engine oil -2 lignosulphate -5 clay - 5, and generally the following is connected to
  • the briquettes have a round lens format with a diameter of 40.5 mm, a height of 28 mm, a moisture content of 3-5%>, a warm supply - 7100-7200 kcal / kg, only 9% a system that testifies to the high quality of products.
  • wood sawn timber for example
  • Briquettes are pressed in the screw process at a pressure of 1, 5 Pa and then the briquettes are dried at 80 ° C for 90 minutes.
  • Received products contain components in the following situation, in wt.%>: Refined engine oil -5 non-sludge -5 non-activated sludge-communicated -8 Consolidated shredded fuel -68
  • the briquettes have a cylinder shape with a diameter of 56 mm, a length of 80 mm, a reliable speed - 4200-4800 kcal / kg, a weight of 5-7%, and a compression of 9 - 9%. testifies to the good quality of the products.
  • the content of coal fines is 35% and the content of fine fines is 35%>.
  • Example 8 Formulated fuels, for example, 7, but in a mixed mixture, the content of dried activated sludge with a water content of 80%, is 49% by weight, and finely divided by weight is 26% by weight. % in the amount of 25 wt.%>, drying was carried out at 120 ° ⁇ for 0.8 hours.
  • Forms have the following composition, in wt.%: Condensed sludge with a special setting with a water content of 10> - 19.8, a mixture of coal fines and a fine mixture of olives is the rest.
  • ⁇ m ⁇ v ⁇ i-b ⁇ i ⁇ e ⁇ y had ⁇ mu and ⁇ azme ⁇ y, ⁇ a ⁇ in ⁇ ime ⁇ e 7 me ⁇ a- niches ⁇ uyu ⁇ chn ⁇ s ⁇ on ⁇ azdavlivanie 6.7-7.2 ⁇ Pa and ⁇ i sb ⁇ asyvanii on si ⁇ e with yachey ⁇ y 25 mm ⁇ s ⁇ aval ⁇ s 85% sb ⁇ asyvaem ⁇ g ⁇ ma ⁇ e ⁇ iala, ch ⁇ svi- de ⁇ els ⁇ vue ⁇ ⁇ vys ⁇ y me ⁇ aniches ⁇ y Particularities.
  • the available capacity of the fuel was 5150 - 5300 kcal / kg, the capacity of the fuel is 1, 03-1, 09 ⁇ / m 1
  • the oil After being dried, the oil must be washed immediately after drying for 5 minutes at a temperature of 80 ° C, and the processed liquid must be cleaned.
  • Formulations have the following composition, in wt.%>: Condensed sludge from a pure installation with a water content of 5% - 13, processed lubricant - 10; mel ⁇ chi mixture of coal and ⁇ sa - ⁇ s ⁇ aln ⁇ e. ⁇ m ⁇ v ⁇ i imeyu ⁇ me ⁇ aniches ⁇ uyu ⁇ chn ⁇ s ⁇ on ⁇ azdavlivanie 6.8-6.6 ⁇ Pa and ⁇ i is ⁇ y ⁇ aves on sb ⁇ asyvanie on si ⁇ e with yachey ⁇ y ⁇ s ⁇ aval ⁇ s 25 mm 88%> sb ⁇ asyvaem ⁇ g ⁇ ma ⁇ e ⁇ iala, ch ⁇ svide ⁇ els ⁇ vue ⁇ ⁇ vys ⁇ y me ⁇ aniches ⁇ y ⁇ chn ⁇ s ⁇ i ⁇ m ⁇ v ⁇ . Density - -
  • the range was 1, 17-1, 19 ⁇ / m / unit; 6350 - 6820 kcal / kg.
  • the feed mixture contains condensed sludge with a water content of 70 ⁇ - 61 wt. ICS and the rest - in equal masses, coal fines and wood sawn, specified components are mixed for 5 minutes in the mixer and the dryer is left for a short time. hours.
  • Forms have the following composition, in wt.%> Condensed sludge with a specific setting with a water content of 11%> - 29.0, a mixture of coal fines and wood waste - other. They come in the form of cylinders in the form of cylinders with a diameter of 25 mm, a length of 25 mm, and they have a tightness of 1, 0-1, 03 t / m and a free range of 5000 - 5180.
  • ⁇ mue maya s ⁇ de ⁇ zhi ⁇ mixture thickened a ⁇ ivny yl s ⁇ de ⁇ zhaniem v ⁇ dy with 80% - 80% by weight and ⁇ s ⁇ aln ⁇ e -.
  • Forms have the following composition, in wt.%: Condensed sludge with a special installation with a water content of 14% ⁇ - 38, a mixture of chopped wooden pastries and dryers.
  • Density was 0.6-0.8 t / m
  • mechanical crushing rate was 12 kg per 1 grater, after 4 dropping grades it was 99%, it was 1.0%. - there is a high mechanical hazard.
  • the free shipping capacity of the fuel is 3530 kcal / kg.
  • the molten fuel has the following composition, in wt.%: Condensed sludge from a specified unit with a water content of 8.5%> - 21; a mixture of oil, sugar and sugar - 25; a mixture of coal fines and wood sawdust - other. Fuel capacity 1, 02 - 1, 05 t / m, quick accessory fuel 4800-4860 fuel oil _ -
  • Formal fuel is sold at a temperature of 1 1, but after drying it at a temperature of 98 ° C, the liquid mixture is not subject to high pressure and the pressure is reduced.
  • the density of the product is 0.8-0.9 t / m ⁇ mechanical pressure is 10–10.5 kg for the discharge, after 4 times the disintegration of 1% - camping, ch ⁇ svide ⁇ els ⁇ vue ⁇ ⁇ b and ⁇ vys ⁇ y me ⁇ aniches ⁇ y ⁇ chn ⁇ s ⁇ i.
  • the spare capacity of the range is 4980 - 5100 kcal / kg.
  • the fuel is suitable for example 10, but drying is carried out only at ambient temperature (26 ° C) for 5 hours.
  • the commercial pressure for crushing is 6.78 - 6.9 PSa, and after 4 times the quick discharge on the system with a 20 mm cell, 86% is lost.
  • the best material for this is the high mechanical properties of the machine.
  • the density of the components is 1, 01 - 1, 04 ⁇ / m 3
  • the spare part capacity is 4200-5050 kcal / kkg.
  • Formal fuel is sold at a temperature of 1 1, but drying is carried out at a temperature of 20–30 ° C for 30 hours.
  • Formulations include, in wt.%>: Condensed sludge from a specific installation with a water content of 10% ⁇ - 34; a mixture of crushed wood skewers, bagasse of dried beets, the core of bakery products - other.
  • the density of the 0.58-0.75 ⁇ / m range is the optional range of 3680 kcal / kg.
  • the commercial size of the pressure for crushing is 14 kg per 1 volume, after 4 quick drops of the speed of 98%, the percentage is 1, 8% This is a testimony to the high mechanical properties of commercial fuel.
  • the fuel is manufactured at example 10, but as a part of the crushed fuel, instead of the fuel, lignin is present.
  • the molten product is sold in wt.%>: Condensed sludge from a specific installation with a water content of 12> - 30; a mixture of coal fines with lignin - the rest.
  • the commercial crushing capacity is 6.8-6.95 PSa, and after 4 quick dumps from a height of 1, 8 meters to the steel plate, With a 20 mm cell, 86-87.5% of the disposable material is left, which indicates a high mechanical impact rating.
  • the feed mixture contains condensed activated sludge with a water content of 15% - 70 wt.% And a fine (0-Zmm) ⁇ with a moisture content of 12% - other.
  • Formulations are contained in wt.%: Condensed sludge with a specific setting with a water content of 10-30%, small t ⁇ - other.
  • Shapes in the form of cylinders with a diameter of 25 mm, a length of 25 mm, have a 0.80-0.82 t / m capacity and an average capacity of 3650-3800 kcal.
  • the commercial size of crushing equipment is 6.15-6.38

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Soil Conditioners And Soil-Stabilizing Materials (AREA)
PCT/RU1998/000219 1998-04-06 1998-07-24 Combustible moule, variantes, et procedes de production de combustible moule WO1999051709A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EA199900319A EA000979B1 (ru) 1998-04-06 1998-07-24 Формованное топливо (варианты) и способы его получения

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
RU98106931 1998-04-06
RU98106931A RU2130047C1 (ru) 1998-04-06 1998-04-06 Топливный брикет и способ его получения
RU98111426 1998-06-15
RU98111426/04A RU2131449C1 (ru) 1998-06-15 1998-06-15 Формованное топливо и способ его получения

Publications (1)

Publication Number Publication Date
WO1999051709A1 true WO1999051709A1 (fr) 1999-10-14

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CZ (1) CZ295727B6 (cs)
EA (1) EA000979B1 (cs)
TR (1) TR199902978T1 (cs)
WO (1) WO1999051709A1 (cs)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1916288A2 (de) 2006-09-25 2008-04-30 Konrad Wieser Verfahren zur Herstellung von Formlingen zur Verbrennung in Pelletbefeuerungsanlagen
RU2418038C2 (ru) * 2009-08-03 2011-05-10 Государственное образовательное учреждение высшего профессионального образования "Кузбасский государственный технический университет" (ГУ КузГТУ) Состав для получения твердого формованного топлива
RU2424280C1 (ru) * 2009-10-30 2011-07-20 Государственное образовательное учреждение высшего профессионального образования "Кузбасский государственный технический университет" (ГУ КузГТУ) Состав для получения формованного топлива
EP2368969A1 (en) 2010-03-15 2011-09-28 Alquimia Soluciones Ambientales S.L. Process for producing non-flammable solid combustible products from flammable products such as industrial residues and solid combustible products obtained therefrom
RU2497935C2 (ru) * 2011-03-14 2013-11-10 Дмитрий Александрович Курьянов Способ получения топливных окатышей
RU2525074C1 (ru) * 2012-12-24 2014-08-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Калининградский государственный технический университет" Высоконаполненный композиционный материал
RU2556226C1 (ru) * 2014-07-02 2015-07-10 Общество с Ограниченной Ответственностью Строительное научно-техническое малое предприятие "ЭЗИП" Топливные брикеты
CZ306924B6 (cs) * 2010-05-14 2017-09-20 Výzkumný ústav zemědělské techniky, v.v.i. Palivo na bázi recyklovaného nebo zbytkového textilu a biomasy
CN109097147A (zh) * 2018-09-13 2018-12-28 中国矿业大学(北京) 一种污泥颗粒燃料及其制备方法
CN113265290A (zh) * 2021-04-27 2021-08-17 深圳市华镛环境工程有限公司 一种有机、纤维固废与污泥掺配制取有机碳燃料配方技术

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WO2015128923A1 (ja) 2014-02-25 2015-09-03 株式会社アクト 乾燥可燃物質の製造方法及び乾燥可燃物質
KR101680957B1 (ko) 2014-03-03 2016-11-29 가부시키가이샤 아이사쿠 고형 연료 제조 장치 및 고형 연료 제조 방법
RU167871U1 (ru) * 2016-04-05 2017-01-11 Федеральное государственное бюджетное образовательное учреждение высшего образования "Тюменский индустриальный университет" (ТИУ) Водонепроницаемые пеллеты
RU2633762C1 (ru) * 2016-12-13 2017-10-18 Федеральное государственное бюджетное образовательное учреждение высшего образования "Казанский государственный энергетический университет" (ФГБОУ ВО "КГЭУ") Способ получения топливных гранул
RU2747049C1 (ru) * 2020-10-01 2021-04-23 Общество с ограниченной ответственностью «Сибнииуглеобогащение» Способ получения бездымного бытового топлива

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Publication number Priority date Publication date Assignee Title
GB1360750A (en) * 1971-11-18 1974-07-24 Metallgesellschaft Ag Method for the abrasion resistance of hot briquettes
GB1465869A (en) * 1975-10-03 1977-03-02 Esmil Envirotech Ltd Method of incinerating sewage sludges
GB1551020A (en) * 1976-12-24 1979-08-22 Refuse Derived Fuels Ltd Preparation of fuels
GB2119813A (en) * 1982-05-08 1983-11-23 Thomas Henry Gardner Production of synthetic solid fuel
GB2133036A (en) * 1982-12-30 1984-07-18 William Frederick Darby Solid fuel and method of manufacture thereof
FR2608167A1 (fr) * 1986-12-15 1988-06-17 Falkenberg Mathias Combustible, procede de preparation de ce combustible et installation pour la mise en oeuvre dudit procede
RU2096442C1 (ru) * 1995-10-17 1997-11-20 Лурий Валерий Григорьевич Способ получения углеродсодержащих брикетов
RU2100415C1 (ru) * 1996-02-20 1997-12-27 Антон Львович Хохлов Состав для брикетированного топлива

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1360750A (en) * 1971-11-18 1974-07-24 Metallgesellschaft Ag Method for the abrasion resistance of hot briquettes
GB1465869A (en) * 1975-10-03 1977-03-02 Esmil Envirotech Ltd Method of incinerating sewage sludges
GB1551020A (en) * 1976-12-24 1979-08-22 Refuse Derived Fuels Ltd Preparation of fuels
GB2119813A (en) * 1982-05-08 1983-11-23 Thomas Henry Gardner Production of synthetic solid fuel
GB2133036A (en) * 1982-12-30 1984-07-18 William Frederick Darby Solid fuel and method of manufacture thereof
FR2608167A1 (fr) * 1986-12-15 1988-06-17 Falkenberg Mathias Combustible, procede de preparation de ce combustible et installation pour la mise en oeuvre dudit procede
RU2096442C1 (ru) * 1995-10-17 1997-11-20 Лурий Валерий Григорьевич Способ получения углеродсодержащих брикетов
RU2100415C1 (ru) * 1996-02-20 1997-12-27 Антон Львович Хохлов Состав для брикетированного топлива

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1916288A2 (de) 2006-09-25 2008-04-30 Konrad Wieser Verfahren zur Herstellung von Formlingen zur Verbrennung in Pelletbefeuerungsanlagen
RU2418038C2 (ru) * 2009-08-03 2011-05-10 Государственное образовательное учреждение высшего профессионального образования "Кузбасский государственный технический университет" (ГУ КузГТУ) Состав для получения твердого формованного топлива
RU2424280C1 (ru) * 2009-10-30 2011-07-20 Государственное образовательное учреждение высшего профессионального образования "Кузбасский государственный технический университет" (ГУ КузГТУ) Состав для получения формованного топлива
EP2368969A1 (en) 2010-03-15 2011-09-28 Alquimia Soluciones Ambientales S.L. Process for producing non-flammable solid combustible products from flammable products such as industrial residues and solid combustible products obtained therefrom
CZ306924B6 (cs) * 2010-05-14 2017-09-20 Výzkumný ústav zemědělské techniky, v.v.i. Palivo na bázi recyklovaného nebo zbytkového textilu a biomasy
RU2497935C2 (ru) * 2011-03-14 2013-11-10 Дмитрий Александрович Курьянов Способ получения топливных окатышей
RU2525074C1 (ru) * 2012-12-24 2014-08-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Калининградский государственный технический университет" Высоконаполненный композиционный материал
RU2556226C1 (ru) * 2014-07-02 2015-07-10 Общество с Ограниченной Ответственностью Строительное научно-техническое малое предприятие "ЭЗИП" Топливные брикеты
CN109097147A (zh) * 2018-09-13 2018-12-28 中国矿业大学(北京) 一种污泥颗粒燃料及其制备方法
CN109097147B (zh) * 2018-09-13 2021-07-23 中国矿业大学(北京) 一种污泥颗粒燃料及其制备方法
CN113265290A (zh) * 2021-04-27 2021-08-17 深圳市华镛环境工程有限公司 一种有机、纤维固废与污泥掺配制取有机碳燃料配方技术

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TR199902978T1 (xx) 2000-10-23
EA199900319A1 (ru) 2000-06-26
EA000979B1 (ru) 2000-08-28
CZ200042A3 (cs) 2000-06-14
CZ295727B6 (cs) 2005-10-12

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