BR102017004819A2 - rsu for production of cdr and or biosynthetic compound for production of synthetic fuel by catalytic depolymerization process kdv and the like. - Google Patents
rsu for production of cdr and or biosynthetic compound for production of synthetic fuel by catalytic depolymerization process kdv and the like. Download PDFInfo
- Publication number
- BR102017004819A2 BR102017004819A2 BR102017004819A BR102017004819A BR102017004819A2 BR 102017004819 A2 BR102017004819 A2 BR 102017004819A2 BR 102017004819 A BR102017004819 A BR 102017004819A BR 102017004819 A BR102017004819 A BR 102017004819A BR 102017004819 A2 BR102017004819 A2 BR 102017004819A2
- Authority
- BR
- Brazil
- Prior art keywords
- production
- kdv
- cdr
- waste
- synthetic
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/40—Thermal non-catalytic treatment
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1011—Biomass
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/04—Diesel oil
-
- 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
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
Abstract
para a melhoria do meio ambiente eliminando os lixões e aterros sanitários do brasil e auxiliando o país a alcançar as metas de produção de combustíveis renováveis, refere-se ao processo de pré-tratamento do resíduo solido urbano para ser utilizado nos processo de gasificação por turbina de fricção utilizando a tecnologia kdv (siglas em alemã para despolimerização catalítica sem pressão) para produção de diesel sintético ou de segunda geração. o objetivo desta invenção é a produção de diesel sintético utilizando a tecnologia de pré-seleção mecânica automática ou manual ou semi-automatizada dos resíduos sólidos urbanos, para produzir um combustível solido derivado de resíduos (cdr), ou um composto biosintético isento de materiais inertes e metais este processo foi determinado pelo fator sustentabilidade ambiental e pelo fator econômico de instalação e operação industrial, sendo que pequenos, médios ou grandes municípios e ou empresas teriam condições de produzir diesel, querosene e nafta sintética com um rendimento energético (kcal) do material da ordem de 80% a partir dos rsu no brasil.for the improvement of the environment by eliminating dumps and landfills in brazil and helping the country to achieve renewable fuel production goals, refers to the process of pre-treatment of solid urban waste to be used in the turbine gasification process of friction using kdv technology (German acronyms for catalytic depolymerization without pressure) for production of synthetic or second generation diesel. The aim of this invention is the production of synthetic diesel using automatic or manual or semi-automated mechanical municipal solid waste pre-selection technology to produce solid waste derived fuel (cdr) or a biosynthetic compound free from inert materials. and metals this process was determined by the environmental sustainability factor and the economic factor of industrial installation and operation, being that small, medium or large municipalities and or companies would be able to produce diesel, kerosene and synthetic naphtha with an energy yield (kcal) of the material. around 80% from the USSR in Brazil.
Description
(54) Título: RSU PARA PRODUÇÃO DE CDR E OU COMPOSTO BIOSINTÉTICO PARA PRODUÇÃO DE COMBUSTÍVEL SINTÉTICO PELO PROCESSO DE DESPOLIMERIZAÇÃO CATALÍTICA KDV E OU SIMILARES.(54) Title: RSU FOR THE PRODUCTION OF CDR AND OR BIOSINTETIC COMPOUND FOR THE PRODUCTION OF SYNTHETIC FUEL BY THE CATALYTIC DEPOLIMERIZATION PROCESS KDV AND SIMILAR.
(51) Int. Cl.: C10B 53/00; C10B 53/07; C10B 53/02; C10G 1/10; C10G 3/00 (73) Titular(es): ENRIQUE EDUARDO ORMEZZANO ENRIQUE ORMEZZANO, CONPROL CONSTRUÇÕES E PROJETOS LTDA.(51) Int. Cl .: C10B 53/00; C10B 53/07; C10B 53/02; 1/10 C10G; C10G 3/00 (73) Owner (s): ENRIQUE EDUARDO ORMEZZANO ENRIQUE ORMEZZANO, CONPROL CONSTRUÇÕES E PROJETOS LTDA.
(72) Inventor(es): ENRIQUE EDUARDO ORMEZZANO (85) Data do Início da Fase Nacional:(72) Inventor (s): ENRIQUE EDUARDO ORMEZZANO (85) Start date of the National Phase:
10/03/2017 (57) Resumo: Para a melhoria do meio ambiente eliminando os lixões e aterros sanitários do Brasil e auxiliando o país a alcançar as metas de produção de combustíveis renováveis, refere-se ao processo de prétratamento do resíduo solido urbano para ser utilizado nos processo de gasificação por turbina de fricção utilizando a tecnologia KDV (siglas em alemã para despolimerização catalítica sem pressão) para produção de diesel sintético ou de segunda geração. O objetivo desta invenção é a produção de diesel sintético utilizando a tecnologia de pré-seleção mecânica automática ou manual ou semi-automatizada dos resíduos sólidos urbanos, para produzir um combustível solido derivado de resíduos (CDR), ou um composto Biosintético isento de materiais inertes e metais este processo foi determinado pelo fator sustentabilidade ambiental e pelo fator econômico de instalação e operação industrial, sendo que pequenos, médios ou grandes municípios e ou empresas teriam condições de produzir diesel, querosene e nafta sintética com um rendimento energético (kcal) do material da ordem de 80% a partir dos RSU no Brasil.03/10/2017 (57) Abstract: For the improvement of the environment by eliminating dumps and sanitary landfills in Brazil and helping the country to reach the renewable fuel production goals, it refers to the process of pretreatment of solid urban waste for be used in friction turbine gasification processes using KDV technology (acronyms in German for non-pressure catalytic depolymerization) for the production of synthetic or second generation diesel. The purpose of this invention is the production of synthetic diesel using automatic or manual or semi-automated mechanical pre-selection technology for municipal solid waste, to produce a solid fuel derived from waste (CDR), or a Biosynthetic compound free of inert materials and metals this process was determined by the environmental sustainability factor and by the economic factor of installation and industrial operation, and small, medium or large municipalities and or companies would be able to produce diesel, kerosene and synthetic naphtha with an energy yield (kcal) of the material 80% from the MSW in Brazil.
RSU PARA PRODUÇÃO DE CDR E OU COMPOSTO BIOSINTÉTICO PARA PRODUÇÃO DE COMBUSTÍVEL SINTÉTICO PELO PROCESSO DE DESPOLIMERIZAÇÃO CATALÍTICA KDV E OU SIMILARES.RSU FOR THE PRODUCTION OF CDR AND OR BIOSINTETIC COMPOUND FOR THE PRODUCTION OF SYNTHETIC FUEL BY THE CATALYTIC DEPOLIMERIZATION PROCESS KDV AND SIMILAR.
01. Setor industrial reciclagem energia renovável.01. Industrial sector recycling renewable energy.
02. A presente invenção refere-se ao processo de utilização de resíduos sólidos urbanos (RSU) para produção de combustível sintético.02. The present invention relates to the process of using urban solid waste (MSW) for the production of synthetic fuel.
03. O pré-tratamento do resíduo solido urbano para ser utilizado nos processo de gasificação por turbina de fricção utilizando a tecnologia KDV (siglas em alemã para despolimerização catalítica sem pressão) patente alemã, para produção de combustível sintético ou de segunda geração, a partir de biomassa.03. The pre-treatment of solid urban waste to be used in gasification processes by friction turbine using KDV technology (acronyms in German for non-pressure catalytic depolymerization) German patent, for the production of synthetic or second generation fuel, from of biomass.
04. Atualmente não existe nenhum processo para a reciclagem total dos resíduos sólidos urbanos, todas as soluções são parciais, lixões, aterros sanitários, ou extremamente custosas, como gaseificação por plasma ou pirólise com baixo rendimento energético.04. Currently, there is no process for the total recycling of solid urban waste, all solutions are partial, dumps, sanitary landfills, or extremely costly, such as plasma gasification or pyrolysis with low energy yield.
05. O objetivo desta invenção é a utilização do lixo municipal para produção de combustível sintético utilizando a tecnologia de pré-seleção mecânica automática ou manual ou semi-automatizada, para produzir um combustível solido derivado de resíduos (CDR) em flocos ou pelletizado ou um composto Biosintético isento de materiais inertes e metais este processo foi determinado pelo fator sustentabilidade ambiental e pelo fator econômico de instalação e operação industrial, sendo que pequenos, médios ou grandes municípios e ou empresas teriam condições de produzir diesel, sintético a partir dos RSU. 06. O Brasil produz 80.000.000 de toneladas ano de lixo que podem ser 100% reciclados e transformados em combustíveis, a rota termoquímica converte a biomassa e os resíduos através de processos como gasificação por fricção e pirólise rápida, a gasificação permite a produção de combustíveis sintéticos muito limpos, que podem ser liquefeitos, este caminho é conhecido como “biomassa-para-líquidos” (BTL - biomassto-liquids ou WTL waste to liquids), o uso de energia continua e intensa, mas a integração de processos promete um aumento de eficiência, na pirólise rápida, a biomassa é rapidamente aquecida (450-600°C), na ausência de ar para render um tipo de óleo combustível pesado - bio-óleo ou óleo de pirólise - que pode ser refinado em vários combustíveis ou usado como tal, altematívamente o bio-óleo e seu resíduo (carvão) 'o.05. The objective of this invention is the use of municipal waste for the production of synthetic fuel using automatic or manual or semi-automated mechanical pre-selection technology, to produce a solid fuel derived from waste (CDR) in flakes or pellets or a Biosynthetic compound free of inert materials and metals This process was determined by the environmental sustainability factor and by the economic factor of installation and industrial operation, and small, medium or large municipalities and or companies would be able to produce diesel, synthetic from the MSW. 06. Brazil produces 80,000,000 tons of garbage per year that can be 100% recycled and transformed into fuels, the thermochemical route converts biomass and waste through processes such as friction gasification and rapid pyrolysis, gasification allows the production of very clean synthetic fuels, which can be liquefied, this path is known as “biomass-to-liquids” (BTL - biomassto-liquids or WTL waste to liquids), the use of continuous and intense energy, but the integration of processes promises a efficiency increase, in rapid pyrolysis, biomass is rapidly heated (450-600 ° C), in the absence of air to yield a type of heavy fuel oil - bio-oil or pyrolysis oil - which can be refined in various fuels or used as such, alternatively bio-oil and its residue (coal) 'o.
w podem ser tratados como uma matéria-prima para produção de combustível BTL, no processo KDV a temperatura de gaseificação esta em tomo de 280°C a 350°C os combustíveis sintéticos têm um balanço de carbono excelente e podem reduzir emissões dc gás carbônico em até 90% quando comparados aos combustíveis de petróleo. Além disso, eles são ultra-limpos e reduzem as emissões dos outros poluidorcs importantes (NOx, SOx), o potencial dos combustíveis baseados em conversão bioquímicas e termoquímica de biomassa é grande. O World Energy Council estimou recentemente que estes combustíveis podem repor aproximadamente 40 por cento de todos os combustíveis de transporte baseados em petróleo, até 2050. Ο 1EA Bioenergia Task 40 vê um potencial maior (até 2050, o que resultaria numa reposição de todos os petrocombustívcis para transporte). Sc o Brasil utiliza-se toda a biomassa residual das agroindústrias, agrosilvipastoril .resíduos da agricultura e RSU teriamos hoje 1.346.000.000 toneladas com capacidade de produção de 471.100.000.000 litros de diesel sintético ano com o processo de despolimerização catalítica KDV isso tomaria o Brasil auto-suficiente em diesel a um custo inferior ao do petróleo, não produzindo dioxina e furanos no processo de gasifícação e tendo um combustível mais limpo com menos enxofre e particulados.w can be treated as a raw material for BTL fuel production, in the KDV process the gasification temperature is around 280 ° C to 350 ° C synthetic fuels have an excellent carbon balance and can reduce carbon dioxide emissions in up to 90% when compared to petroleum fuels. In addition, they are ultra-clean and reduce emissions from the other major polluters (NOx, SOx), the potential of fuels based on biochemical and biomass thermo-chemical conversion is great. The World Energy Council recently estimated that these fuels can replace approximately 40 percent of all petroleum-based transport fuels by 2050. EA 1EA Bioenergy Task 40 sees greater potential (by 2050, which would result in a replacement of all petroleum fuels for transportation). If Brazil uses all the residual biomass from agro-industries, agrosilvipastoral. Agricultural waste and MSW we would have today 1,346,000,000 tons with a production capacity of 471,100,000,000 liters of synthetic diesel per year with the KDV catalytic depolymerization process that would take Brazil self-sufficient in diesel at a lower cost than oil, not producing dioxin and furans in the gasification process and having a cleaner fuel with less sulfur and particulates.
07. Os combustíveis gerados a partir de resíduos e materiais biologicamente recicláveis representam uma alternativa para o aumento da produção para o futuro da tecnologia energética descentralizada; O pré-tratamento da biomassa como se menciono anteriormente, a plataforma termoquímica compreende a obtenção do gás de síntese (syngas) a partir de gaseificação da biomassa para a produção de bicombustiveis de segunda geração, entre eles o biodiesel sintético porem essa biomassa a ser utilizada precisa ser pré-tratada antes de entrar no processo, as técnicas do pré-tratamento são a estocagem que pode ser critica no pré-tratamento dos resíduos, cia deve scr adequada para garantir o fornecimento constante, evitar mudanças nas características fundamentais da matéria prima (apodrecimento, deterioração, etc.).07. Fuels generated from waste and biologically recyclable materials represent an alternative for increasing production for the future of decentralized energy technology; The pre-treatment of biomass as mentioned above, the thermochemical platform comprises obtaining the synthesis gas (syngas) from biomass gasification for the production of second generation biofuels, including synthetic biodiesel, however this biomass to be used it needs to be pre-treated before entering the process, the pre-treatment techniques are the storage that can be critical in the pre-treatment of waste, it must be adequate to ensure constant supply, avoid changes in the fundamental characteristics of the raw material ( decay, deterioration, etc.).
<2 cr<2 cr
F|SF | S
RubRub
3/43/4
08. A pré seleção separa os materiais inorgânicos inertes (vidro, cerâmica, restos de terras, metais, eletroeletrônicos) utiliza um equipamento chamado abridor de sacos, peneiras de classificação granulométrica e por vibração ou rotativa , para separar os restos de alimentos dos demais materiais,a separação automática e para grandes volumes de lixo utiliza para classificar sistemas eletromagnéticos para metais ferrosos, de indução para metais não-ferrosos, de leitura ótica e infravermelho, de densidade por corrente de ar para plásticos e papéis e manuais para pequenas usinas (catação), os processos de compactação de biomassa são vários como trituração e moagem essas operações unitárias são usadas para a redução e uniformização do tamanho das partículas, no caso da gaseificação por turbina de fricção KDV esse tamanho deve estar entre 0 - 25mm equipamentos como picadorcs dc toras, moinhos dc bola, moinhos dc facas e moinhos martelo, a secagem nos processos térmicos e desejável que o resíduos sejam secos ou tenham umidade compatível podendo variar entre 8% a 15%, e para isso há necessidade do uso de energia, muitos processos têm geralmente excedente de energia térmica que pode ser usada para secagem, embora o Brasil a industria canavieira tenha se especializado na queima de bagaço com alta umidade, outros processos de conversão termoquímica como a pirólise rápida e a gaseificação por turbina de fricção KDV trabalham geralmente com teores de umidade (<20%) isso significa que o combustível derivado do resíduo (CDR) e a matéria orgânica (restos de alimentos, etc.) terão que ser submetidos a desidratação o ao processo de desidratação e fusão molecular utilizando uma aglutinadora de plástico dando lugar a um material inerte composto Biosintético com limites de 0% - 50% de matérias plásticas como PET, PP, PE, PVC, e outros tipos de plásticos, borrachas, pneus,isopor, óleos vegetais e ou minerais usados. 09. O limite do teor de umidade terá que ser na faixa de <1% - 20% para processar o material nas unidades KDV para obtenção dc dicscl sintético. A compactação serve para otimizar o espaço utilizado para estocagem em forma de fardos, briquetes e pelletizados, também aumentando a densidade energética melhorando através destes processos o rendimento das usinas KDV e tomando o lixo inerte, podendo estocar o mesmo sem08. Pre-selection separates inert inorganic materials (glass, ceramics, earth scraps, metals, electronics) uses equipment called a bag opener, granulometric and vibrating or rotating sieves to separate food waste from other materials , automatic separation and for large volumes of waste uses to classify electromagnetic systems for ferrous metals, induction for non-ferrous metals, optical and infrared reading, airflow density for plastics and papers and manuals for small plants (scavenging ), the biomass compaction processes are various such as crushing and grinding these unit operations are used to reduce and standardize the size of the particles, in the case of gasification by friction turbine KDV this size must be between 0 - 25mm equipment such as dc choppers logs, ball mills, knife mills and hammer mills, drying in thermal processes and it is desirable that the resin both are dry or have compatible humidity, which can vary between 8% to 15%, and for that there is a need for the use of energy, many processes generally have surplus of thermal energy that can be used for drying, although in Brazil the sugar industry has specialized in burning bagasse with high humidity, other thermochemical conversion processes such as rapid pyrolysis and gasification by KDV friction turbine generally work with moisture content (<20%) this means that the fuel derived from the waste (CDR) and the material organic (leftover food, etc.) will have to be subjected to dehydration or to the process of dehydration and molecular fusion using a plastic binder giving way to an inert composite Biosynthetic material with limits of 0% - 50% of plastic materials like PET, PP, PE, PVC, and other types of used plastics, rubbers, tires, styrofoam, vegetable oils and or minerals. 09. The moisture content limit must be in the range of <1% - 20% to process the material in the KDV units to obtain synthetic dicscl. The compaction serves to optimize the space used for storage in the form of bales, briquettes and pellets, also increasing the energy density, improving through these processes the performance of KDV plants and taking inert waste, being able to store it without
4/4 prejuízo ao meio ambiente, viabilizando grandes e pequenos empreendimentos, possibilitando a geração de empregos, eliminando definitivamente não só os lixões como também os aterros sanitários que mesmo sendo controlados geram poluição e a utilização de grandes extensões de terras que ficam contaminadas e produzindo Chorume c gás metano na atmosfera pcrmancntcmcntc.4/4 damage to the environment, enabling large and small enterprises, enabling the generation of jobs, definitively eliminating not only landfills but also landfills that, even if controlled, generate pollution and the use of large areas of land that are contaminated and producing Slurry and methane gas in the atmospheric atmosphere.
10. É a junção de dois processos tomando-o um sistema sustentável economicamente, ambientalmente e socialmente.10. It is the joining of two processes making it a sustainable system economically, environmentally and socially.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BR102017004819A BR102017004819A2 (en) | 2017-03-10 | 2017-03-10 | rsu for production of cdr and or biosynthetic compound for production of synthetic fuel by catalytic depolymerization process kdv and the like. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BR102017004819A BR102017004819A2 (en) | 2017-03-10 | 2017-03-10 | rsu for production of cdr and or biosynthetic compound for production of synthetic fuel by catalytic depolymerization process kdv and the like. |
Publications (1)
Publication Number | Publication Date |
---|---|
BR102017004819A2 true BR102017004819A2 (en) | 2018-10-30 |
Family
ID=64268886
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR102017004819A BR102017004819A2 (en) | 2017-03-10 | 2017-03-10 | rsu for production of cdr and or biosynthetic compound for production of synthetic fuel by catalytic depolymerization process kdv and the like. |
Country Status (1)
Country | Link |
---|---|
BR (1) | BR102017004819A2 (en) |
-
2017
- 2017-03-10 BR BR102017004819A patent/BR102017004819A2/en not_active Application Discontinuation
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US10961459B2 (en) | System for production of a renewable liquid fuel | |
US11345860B2 (en) | System and method for continuous production of a renewable liquid fuel | |
Lacey et al. | Removal of introduced inorganic content from chipped forest residues via air classification | |
Kundu et al. | Thermochemical conversion of biomass to bioenergy: a review | |
US20170369806A1 (en) | Green renewable liquid fuel | |
Abdoli et al. | Wood Pellet as a Renewable Source of Energy | |
Rahman et al. | Chemical composition and physical characteristics of coal and mangrove wood as alternative fuel | |
US20240101907A1 (en) | Process for a plastic product conversion | |
Sharma et al. | Environmentally friendly fuel obtained from pyrolysis of waste tyres | |
Samal et al. | Char from the co-pyrolysis of Eucalyptus wood and low-density polyethylene for use as high-quality fuel: Influence of process parameters | |
Salimbeni | Organic waste streams upgrading for gasification process optimization | |
BR102017004819A2 (en) | rsu for production of cdr and or biosynthetic compound for production of synthetic fuel by catalytic depolymerization process kdv and the like. | |
Onyango | Pyrolysis: an alternative technology for municipal solid waste management | |
Putra et al. | Conversion of organic fraction of municipal solid waste into solid fuel via hydrothermal carbonization | |
RU2008149215A (en) | FUEL SYSTEM AND METHOD FOR PRODUCING IT | |
Sakthivel et al. | Waste to liquid fuels: potency, progress and challenges | |
KR101065390B1 (en) | Method for manufacturing solid bio-charcoal of environment-friendly low carbon green growth by utilizing industrial organic wastes, and the solid bio-charcoal produced thereof | |
Hamzah et al. | Woody biomass characterization for 100 megawatt-hours (MW) power generation | |
NL2026522B1 (en) | Process for a plastic product conversion | |
Tihin et al. | Overview of municipal solid wastes-derived refuse-derived fuels for cement co-processing | |
Sherzodbek et al. | TREATMENT OF SOLID WASTE | |
Rubiera et al. | Raw materials, selection, preparation and characterization | |
Abdullayev et al. | Treatment of Solid Waste | |
Maneses et al. | Critical analysis of material and energy recovery processes of municipal solid waste in Satu Mare county | |
Sen et al. | An integrated approach to the utilization of low rank coals and biofuel |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
B03A | Publication of an application: publication of a patent application or of a certificate of addition of invention | ||
B11A | Dismissal acc. art.33 of ipl - examination not requested within 36 months of filing | ||
B11Y | Definitive dismissal acc. article 33 of ipl - extension of time limit for request of examination expired |