Coal is a very prominent energy source in the world, but it is environmentally unattractive due to its high sulfur and ash content as well as its alleged contribution towards climate change, but it is affordable, abundant, and has high energy content. Thus, utilizing coal in a cleaner and more efficient way has become necessary. One promising clean coal technology involves fully gasifying coal into synthesis gas, cleaning it, and feeding it into a high-efficiency combined cycle, such as an Integrated Gasification Combined Cycle (IGCC). Inspired by the recent success of warn gas cleanup (WGCU), mild and partial gasification are proposed as less energy intensive options. This Integrated Mild/Partial Gasification Combined Cycle (IMPGC) could significantly save energy and improve efficiency. The objective of this study is to investigate the capabilities of IMPGC as both a new plant and a retrofit option for traditional coal power plants with and without carbon capture. I MPGC relies on the principles of mild and partial gasification and the recently available WGGU technology with the following benefits: a.) completely negate the need for syngas cooling; b.) significantly reduce the energy needed to fully thermally crack the volatiles and completely gasify the char as in the IGCC system; c.) preserve the high chemical energy hydro-carbon bonds within the feedstock to allow more efficient combustion in the gas turbine; d.) reduce the size of gasifier and piping to reduce the costs; and e.) enable retrofitting of an old coal power plant by preserving the existing equipment. The software used (Thermoflex®) was first validated with established cases from the U.S. Department of Energy. For new plants, the results show that IMPGC’s efficiency is 8 percentage points (20%) higher than IGCC, 8 points higher than a modern subcritical Rankine cycle, and 3-4 points higher than an ultra-supercritical (USC) cycle. When retrofitting older plants, a minimum improvement of over 4 points is predicted. When carbon capture is involved, IMPGC’s efficiency becomes 10 points better than a subcritical plant and 8 points better than a USC plant. Emissions wise, IMPGC is better than IGCC and much better than Rankine cycle plants.

The thermodynamic properties of CO2-mixtures are essential for the design and operation of CO2 Capture and Storage (CCS) systems. A better understanding of the thermodynamic properties of CO2 mixtures could provide a scientific basis to define a proper guideline of CO2 purity and impure components for the CCS processes according to technical, safety and environmental requirements. However the available accurate experimental data cannot cover the whole operation conditions of CCS processes. In order to overcome the shortage of experimental data, theoretical estimation and modelling are used as a supplemental approach.   In this thesis, the available experimental data on the thermodynamic properties of CO2 mixtures were first collected, and their applicability and gaps for theoretical model verification and calibration were also determined according to the required thermodynamic properties and operation conditions of CCS. Then in order to provide recommendations concerning calculation methods for engineering design of CCS, totally eight equations of state (EOS) were evaluated for the calculations about vapour liquid equilibrium (VLE) and density of CO2-mixtures, including N2, O2, SO2, Ar, H2S and CH4.   With the identified equations of state, the preliminary assessment of impurity impacts was further conducted regarding the thermodynamic properties of CO2-mixtures and different processes involved in CCS system. Results show that the increment of the mole fraction of non-condensable gases would make purification, compression and condensation more difficult. Comparatively N2 can be separated more easily from the CO2-mixtures than O2 and Ar. And a lower CO2 recovery rate is expected for the physical separation of CO2/N2 under the same separation conditions. In addition, the evaluations about the acceptable concentration of non-condensable impurities show that the transport conditions in vessels are more sensitive to the non-condensable impurities and it requires very low concentration of non-condensable impurities in order to avoid two-phase problems.   Meanwhile, the performances of evaporative gas turbine integrated with different CO2 capture technologies were investigated from both technical and economical aspects. It is concluded that the evaporative gas turbine (EvGT) cycle with chemical absorption capture has a smaller penalty on electrical efficiency, while a lower CO2 capture ratio than the EvGT cycle with O2/CO2 recycle combustion capture. Therefore, although EvGT + chemical absorption has a higher annual cost, it has a lower cost of electricity because of its higher efficiency. However considering its lower CO2 capture ratio, EvGT + chemical absorption has a higher cost to avoid 1 ton CO2. In addition the efficiency of EvGT + chemical absorption can be increased by optimizing Water/Air ratio, increasing the operating pressure of stripper and adding a flue gas condenser condensing out the excessive water. / QC 20100819

Coal-fired power plants are the largest anthropogenic point sources of CO2 emissions worldwide. About 40% of the world's electricity comes from coal. Approximately 49% of the US electricity in 2008 and 23% of the total electricity generation of Canada in 2000 came from coal-fired power plant (World Coal Association, and Statistic Canada). It is likely that in the near future there might be some form of CO2 regulation. Therefore, it is highly probable that CO2 capture will need to be implemented at many US and Canadian coal fired power plants at some point. Several technologies are available for CO2 capture from coal-fired power plants. One option is to separate CO2 from the combustion products using conventional approach such as chemical absorption/stripping with amine solvents, which is commercially available. Another potential alternative, membrane gas separation, involves no moving parts, is compact and modular with a small footprint, is gaining more and more attention. Both technologies can be retrofitted to existing power plants, but they demands significant energy requirement to capture, purify and compress the CO2 for transporting to the sequestration sites. This thesis is a techno-economical evaluation of the two approaches mentioned above along with another approach known as hybrid. This evaluation is based on the recent advancement in membrane materials and properties, and the adoption of systemic design procedures and optimization approach with the help of a commercial process simulator. Comparison of the process performance is developed in AspenPlus process simulation environment with a detailed multicomponent gas separation membrane model, and several rigorous rate-based absorption/stripping models. Fifteen various single and multi-stage membrane process configurations with or without recycle streams are examined through simulation and design study for industrial scale post-combustion CO2 capture. It is found that only two process configurations are capable to satisfy the process specifications i.e., 85% CO2 recovery and 98% CO2 purity for EOR. The power and membrane area requirement can be saved by up to 13% and 8% respectively by the optimizing the base design. A post-optimality sensitivity analysis reveals that any changes in any of the factors such as feed flow rate, feed concentration (CO2), permeate vacuum and compression condition have great impact on plant performance especially on power consumption and product recovery. Two different absorption/stripping process configurations (conventional and Fluor concept) with monoethanolamine (30 wt% MEA) solvent were simulated and designed using same design basis as above with tray columns. Both the rate-based and the equilibrium-stage based modeling approaches were adopted. Two kinetic models for modeling reactive absorption/stripping reactions of CO2 with aqueous MEA solution were evaluated. Depending on the options to account for mass transfer, the chemical reactions in the liquid film/phase, film resistance and film non-ideality, eight different absorber/stripper models were categorized and investigated. From a parametric design study, the optimum CO2 lean solvent loading was determined with respect to minimum reboiler energy requirement by varying the lean solvent flow rate in a closed-loop simulation environment for each model. It was realized that the success of modeling CO2 capture with MEA depends upon how the film discretization is carried out. It revealed that most of the CO2 was reacted in the film not in the bulk liquid. This insight could not be recognized with the traditional equilibrium-stage modeling. It was found that the optimum/or minimum lean solvent loading ranges from 0.29 to 0.40 and the reboiler energy ranges from 3.3 to 5.1 (GJ/ton captured CO2) depending on the model considered. Between the two process alternatives, the Fluor concept process performs well in terms of plant operating (i.e., 8.5% less energy) and capital cost (i.e., 50% less number of strippers). The potentiality of hybrid processes which combines membrane permeation and conventional gas absorption/stripping using MEA were also examined for post-combustion CO2 capture in AspenPlus®. It was found that the hybrid process may not be a promising alternative for post-combustion CO2 capture in terms of energy requirement for capture and compression. On the other hand, a stand-alone membrane gas separation process showed the lowest energy demand for CO2 capture and compression, and could save up to 15 to 35% energy compare to the MEA capture process depending on the absorption/stripping model used.

As is now generally accepted, climate change and environmental degradation has largely been triggered by carbon emissions and energy modeling for policy analysis has therefore attained renewed urgency. It is important for governments to satisfy emission targets and timetables set down by international agreements without disregarding macroeconomic concerns and restrictions. In this study, we present a large-scale nonlinear optimization model that allows the analysis of macroeconomic and multi-sectoral energy policies in respect of technological and environmental options and scenarios. The model consists of a detailed representation of energy activities and disaggregates the rest of the economy into five main sectors. Economy-wide solutions are obtained by computing a utility maximizing aggregate consumption bundle on the part of a representative household. Intersectoral and foreign transaction balances are maintained using a modified accounting matrix. The model also computes the impact on macroeconomic variables of greenhouse gas (GHG) emission strategies and abatement schemes. As such the model is capable of producing solutions that can be used to benchmark regulatory instruments and policies. Several scenarios are presented for the case of Turkey in which the impact of a nuclear power programme and power generation coupled with carbon-capture-and-storage schemes are investigated as well as setting quotas on total and sectoral GHG emissions.

Once a source of environmental concern, mine tailings could now contribute to the fight against climate change. Greg Dipple and team are discovering how mines can potentially ofset their own emissions.

Coal-fired power plants are the largest anthropogenic point sources of CO2 emissions worldwide. About 40% of the world's electricity comes from coal. Approximately 49% of the US electricity in 2008 and 23% of the total electricity generation of Canada in 2000 came from coal-fired power plant (World Coal Association, and Statistic Canada). It is likely that in the near future there might be some form of CO2 regulation. Therefore, it is highly probable that CO2 capture will need to be implemented at many US and Canadian coal fired power plants at some point. Several technologies are available for CO2 capture from coal-fired power plants. One option is to separate CO2 from the combustion products using conventional approach such as chemical absorption/stripping with amine solvents, which is commercially available. Another potential alternative, membrane gas separation, involves no moving parts, is compact and modular with a small footprint, is gaining more and more attention. Both technologies can be retrofitted to existing power plants, but they demands significant energy requirement to capture, purify and compress the CO2 for transporting to the sequestration sites. This thesis is a techno-economical evaluation of the two approaches mentioned above along with another approach known as hybrid. This evaluation is based on the recent advancement in membrane materials and properties, and the adoption of systemic design procedures and optimization approach with the help of a commercial process simulator. Comparison of the process performance is developed in AspenPlus process simulation environment with a detailed multicomponent gas separation membrane model, and several rigorous rate-based absorption/stripping models. Fifteen various single and multi-stage membrane process configurations with or without recycle streams are examined through simulation and design study for industrial scale post-combustion CO2 capture. It is found that only two process configurations are capable to satisfy the process specifications i.e., 85% CO2 recovery and 98% CO2 purity for EOR. The power and membrane area requirement can be saved by up to 13% and 8% respectively by the optimizing the base design. A post-optimality sensitivity analysis reveals that any changes in any of the factors such as feed flow rate, feed concentration (CO2), permeate vacuum and compression condition have great impact on plant performance especially on power consumption and product recovery. Two different absorption/stripping process configurations (conventional and Fluor concept) with monoethanolamine (30 wt% MEA) solvent were simulated and designed using same design basis as above with tray columns. Both the rate-based and the equilibrium-stage based modeling approaches were adopted. Two kinetic models for modeling reactive absorption/stripping reactions of CO2 with aqueous MEA solution were evaluated. Depending on the options to account for mass transfer, the chemical reactions in the liquid film/phase, film resistance and film non-ideality, eight different absorber/stripper models were categorized and investigated. From a parametric design study, the optimum CO2 lean solvent loading was determined with respect to minimum reboiler energy requirement by varying the lean solvent flow rate in a closed-loop simulation environment for each model. It was realized that the success of modeling CO2 capture with MEA depends upon how the film discretization is carried out. It revealed that most of the CO2 was reacted in the film not in the bulk liquid. This insight could not be recognized with the traditional equilibrium-stage modeling. It was found that the optimum/or minimum lean solvent loading ranges from 0.29 to 0.40 and the reboiler energy ranges from 3.3 to 5.1 (GJ/ton captured CO2) depending on the model considered. Between the two process alternatives, the Fluor concept process performs well in terms of plant operating (i.e., 8.5% less energy) and capital cost (i.e., 50% less number of strippers). The potentiality of hybrid processes which combines membrane permeation and conventional gas absorption/stripping using MEA were also examined for post-combustion CO2 capture in AspenPlus®. It was found that the hybrid process may not be a promising alternative for post-combustion CO2 capture in terms of energy requirement for capture and compression. On the other hand, a stand-alone membrane gas separation process showed the lowest energy demand for CO2 capture and compression, and could save up to 15 to 35% energy compare to the MEA capture process depending on the absorption/stripping model used.

Líquidos iônicos imidazólios (LIIs) associados a ânions com caráter básico foram sintetizados, caracterizados e seu comportamento estudado em solução. Inicialmente a troca isotópica H/D preferencial no grupo C2-CH3 de sais de 1-nbutil-2,3-dimetilimidazólio (BMMI) foi avaliada. Ficou evidente que o contato entre os pares de íons e a atuação do ânion como uma base neutra influenciaram fortemente a deuteração. Após a análise dos resultados de RMN, cálculos de DFT (Teoria do Funcional de Densidade) e Difração de Raios X, um complexo entre uma molécula de água e alguns LI foi sugerido, modificando fortemente a estrutura organizacional e afetando também a troca isotópica nestes sais. Através do mecanismo reacional proposto, surgiu a possibilidade de deuteração de novos substratos contendo H ácidos, usando os LIIs como catalisadores. A reação de troca isotópica em alcinos e cetonas foi estudada e bons resultados foram obtidos. O efeito da variação de cátions e ânions na atividade catalítica foi analisado, assim como a variação dos substituintes dos substratos. Além disso, um estudo cinético foi realizado através de análises de RMN de 1H e o mecanismo reacional foi proposto. Por fim, a capacidade de formação de pares iônicos em soluções aquosas de LIIs foi avaliada na captura de CO2. Ótimos resultados foram obtidos e atribuídos à ocorrência de sorção física e química devido à ativação da água pelo LII. / Imidazolium based ionic liquids (ImIL) associated with basic anions were synthesized, characterized and studied. Initially the preferred H/D isotopic exchange to C2-CH3 group of 1-nbutyl-2,3-dimethylimidazolium salts (BMMI) was studied. In this context, it became evident that the ion-pairing formation and the anion action as a neutral base strongly influence the deuteration reaction. NMR analysis, theoretical calculation (Density Functional Theory) and X-ray Diffraction have been performed and a complex between a water molecule and the IL have been suggested, strongly modifying the IL structure and characteristics. The isotope exchange reaction in alkynes and ketones was studied using imidazolium based ionic liquids as catalysts and good results obtained. The effect of cation and anion variation on the catalyst activity were analyzed, also a variation of the substrate substituent’s. Also, a kinetic study was performed by 1H NMR analyzes and the reaction mechanism were proposed. Finally, the ability to form ion pair contact of ILs in aqueous solutions was evaluated for CO2 capture. Great results were obtained and this success can be attributed to the occurrence of physical and chemical sorption due to water activation by the IL.

Les clathrates organiques, particulièrement ceux formés entre l’hydroquinone (HQ) et les gaz, sont des entités supramoléculaires montrant un potentiel intéressant comme matériau alternatif pour les applications de stockage et de séparation de gaz. Cette étude traite de l’évaluation du clathrate d’HQ pour la séparation du CO2 contenu dans les mélanges CO2/CH4 par réaction gaz-solide. D’un point de vue fondamental, différentes propriétés des clathrates d’HQ-CO2, -CO2/CH4 et -CH4 ont été analysées: signatures spectroscopiques, structures cristallines, morphologies, capacités de stockage de gaz, températures de relargage de gaz et températures de transition structurales. Ce travail offre aussi de nouveaux éléments de compréhension des mécanismes de formation et de dissociation des clathrates d’HQ. Il est montré que, pour capturer efficacement et sélectivement le CO2, la réaction d’enclathration doit être faite en utilisant l’intermédiaire « clathrate vide » formé à partir du clathrate d’HQ-CO2. D’un point de vue pratique, les courbes d’équilibre, les enthalpies de dissociation, et les occupations dans les conditions d’équilibre ont été déterminées pour les clathrates d’HQ-CO2 et -CH4 dans une gamme étendue de température allant de 288 à 354 K. De plus, la cinétique de la réaction d’enclathration a été étudiée expérimentalement et modélisée. Dans cette optique, un matériau composite à base d’hydroquinone a été développé, et permet de capter et stocker le gaz de manière réversible, et d’améliorer significativement la cinétique d’enclathration. Le procédé de séparation de gaz basé sur la formation du clathrate d’hydroquinone a aussi été étudié. L’influence des paramètres opératoires (i.e. temps de réaction, pression, température et composition du gaz d’alimentation) sur la cinétique de capture, la sélectivité et la capacité de stockage de gaz ont été évaluées à travers des expériences menées à l’échelle pilote. / Organic clathrate compounds, particularly those formed between hydroquinone (HQ) and gases, are supramolecular entities recently highlighted as promising alternatives for applications such as gas storage and separation processes. This study deals with an evaluation of the HQ clathrates to separate CO2 from CO2/CH4 gas mixtures through direct gas-solid reaction. On the fundamental point of view, new insights into several properties of the CO2-, CO2/CH4-, and CH4-HQ clathrates were studied: spectroscopic signatures, crystal structures, morphologies, gas storage capacities, guest release temperatures and structural transition temperatures. This work also offers new elements of understanding HQ clathrate formation and dissociation mechanisms. It is shown that, for capturing CO2 the most selectively and efficiently, the enclathration reaction has to be done with the “guest-free intermediate” derived from the CO2−HQ clathrates. On a practical point of view, the equilibrium curves, the dissociation enthalpies, and the occupancies at the equilibrium clathrate forming conditions, were determined for the CO2- and CH4-HQ clathrates in an extended range of temperature from about 288 to 354 K. Moreover, the kinetics of the gas-solid enclathration reaction were studied experimentally and modelled. In this way, HQ-based composite materials were developed and allows to reversibly capture and store gases, and to significantly improve the enclathration kinetics. The hydroquinone clathrate based gas separation (HCBGS) process was also investigated. The influence of the process operating parameters (i.e. reaction time, pressure, temperature and feed gas composition) on the CO2 capture kinetics, the selectivity toward CO2, and the storage capacity were assessed through experiments performed at pilot scale.

O Painel Intergovernamental de Mudanças Climáticas da ONU (IPCC) tem comprovado com nível de confiança cada vez maior, ao longo dos últimos anos, a forte relação entre o aumento da temperatura média global e o aumento dos gases de efeito estufa (GEEs) principalmente quanto ao gás que mais contribui para a composição desses gases: o gás carbônico ou CO2. O Brasil se insere no rol dos emissores desse gás, principalmente devido ao desmatamento das reservas florestais que possui. Assim, assumiu o compromisso na Convenção Quadro das Nações Unidas sobre Mudanças Climáticas (United Nations Framework Convention on Climate Change UNFCCC) de estabilizar suas emissões e inventariar periodicamente os seus GEEs. Dentro deste contexto, cabe também à indústria levantar sua parcela de responsabilidade significativa neste processo ameaçador para a vida no planeta terra. Desta forma, o principal objetivo do presente trabalho foi o de levantar e contabilizar o Inventário dos GEEs emitidos em 2006 por uma empresa que produz importantes insumos para a indústria de petróleo. A pesquisa bibliográfica sobre a metodologia mais adequada e sua aplicação para a empresa em estudo foram os principais objetivos específicos. A autora não encontrou fatores de emissão de CO2 (kg CO2/TJ do combustível, detalhado no decorrer deste trabalho) desenvolvidos no Brasil para levantar o inventário, com um nível razoável de confiança, que reflita a situação real e local. Toda a pesquisa bibliográfica feita mostrou que os trabalhos realizados mesmo por órgãos governamentais brasileiros usaram a metodologia do IPCC (versão anterior à usada neste trabalho) que foi elaborada por países desenvolvidos, que não é o nosso caso ou realidade. Foram feitas diversas visitas à empresa, levantadas todas as fontes potenciais de emissão, consumos e características de todos os combustíveis usados, bem como o levantamento do trabalho desenvolvido sobre geração de mudas de plantas no seu horto. Através de cálculos por essa metodologia reconhecida mundialmente (IPCC) a autora encontrou um valor em torno de 76.000 toneladas de CO2 emitidos pela empresa em 2006. A empresa neutralizou cerca de 80 toneladas de CO2, através da produção de mudas (para doação e plantio em torno de uma área que é um passivo ambiental) em seu horto e o que plantou na área desse passivo em 2006. Isso significou cerca de 0,1% do que emitiu / The Intergovernamental Panel Climate Change - IPCC from ONU has proved with higher level of confidence, along last years, a strong relation between the global average temperature increasing and the Greenhouse Gases increasing mainly about the biggest contributor to the composition in these gases: the carbonic gas or CO2. Brazil is included in the list of these gas polluters, mainly because of its deforestation. Then, it assumed the commitment with United Nations Framework Convention on Climate Change UNFCCC of stabilize and calculate his Greenhouse Gases (GHG) Inventory. In this context, the industries must to survey their part of responsibility in this threatening process for the life in this planet. For the reasons above, the main purpose from the present work is to calculate the Greenhouse Gases emissions inventory in 2006 from a enterprise that produces important inputs for a petroleum industry. The specific purposes were to research the bibliography about the most suitable methodology and its application for this enterprise. The author of this work didnt find any emission factors for CO2 developed in Brazil for calculate the inventory, with a reasonable level of confidence, which can show the real and local situation about this subject. Then, the entire bibliographic search done showed that the works found even in governmental institutions used the IPCC methodology, done by developed countries, that isnt our reality. For this study, it was done several visits to that enterprise and identified all the sources from these GHG, fuel uses and their quantities and intensive bibliographic searches about several national and international methodologies. It was seen the developed work done by this enterprise about generation of seedling (plants) in its market garden. It was chosen the IPCC methodology that was the tool to calculate about 76.000 t of CO2 emitted by the enterprise in 2006. This studied enterprise neutralized 80 t of CO2, through the production of plants cuttings (for donation to people and to plant in around an area that is an environmental passive) in its market garden and what it planted in that passive area in 2006. This was about 0,1% on that it emitted

O Painel Intergovernamental de Mudanças Climáticas da ONU (IPCC) tem comprovado com nível de confiança cada vez maior, ao longo dos últimos anos, a forte relação entre o aumento da temperatura média global e o aumento dos gases de efeito estufa (GEEs) principalmente quanto ao gás que mais contribui para a composição desses gases: o gás carbônico ou CO2. O Brasil se insere no rol dos emissores desse gás, principalmente devido ao desmatamento das reservas florestais que possui. Assim, assumiu o compromisso na Convenção Quadro das Nações Unidas sobre Mudanças Climáticas (United Nations Framework Convention on Climate Change UNFCCC) de estabilizar suas emissões e inventariar periodicamente os seus GEEs. Dentro deste contexto, cabe também à indústria levantar sua parcela de responsabilidade significativa neste processo ameaçador para a vida no planeta terra. Desta forma, o principal objetivo do presente trabalho foi o de levantar e contabilizar o Inventário dos GEEs emitidos em 2006 por uma empresa que produz importantes insumos para a indústria de petróleo. A pesquisa bibliográfica sobre a metodologia mais adequada e sua aplicação para a empresa em estudo foram os principais objetivos específicos. A autora não encontrou fatores de emissão de CO2 (kg CO2/TJ do combustível, detalhado no decorrer deste trabalho) desenvolvidos no Brasil para levantar o inventário, com um nível razoável de confiança, que reflita a situação real e local. Toda a pesquisa bibliográfica feita mostrou que os trabalhos realizados mesmo por órgãos governamentais brasileiros usaram a metodologia do IPCC (versão anterior à usada neste trabalho) que foi elaborada por países desenvolvidos, que não é o nosso caso ou realidade. Foram feitas diversas visitas à empresa, levantadas todas as fontes potenciais de emissão, consumos e características de todos os combustíveis usados, bem como o levantamento do trabalho desenvolvido sobre geração de mudas de plantas no seu horto. Através de cálculos por essa metodologia reconhecida mundialmente (IPCC) a autora encontrou um valor em torno de 76.000 toneladas de CO2 emitidos pela empresa em 2006. A empresa neutralizou cerca de 80 toneladas de CO2, através da produção de mudas (para doação e plantio em torno de uma área que é um passivo ambiental) em seu horto e o que plantou na área desse passivo em 2006. Isso significou cerca de 0,1% do que emitiu / The Intergovernamental Panel Climate Change - IPCC from ONU has proved with higher level of confidence, along last years, a strong relation between the global average temperature increasing and the Greenhouse Gases increasing mainly about the biggest contributor to the composition in these gases: the carbonic gas or CO2. Brazil is included in the list of these gas polluters, mainly because of its deforestation. Then, it assumed the commitment with United Nations Framework Convention on Climate Change UNFCCC of stabilize and calculate his Greenhouse Gases (GHG) Inventory. In this context, the industries must to survey their part of responsibility in this threatening process for the life in this planet. For the reasons above, the main purpose from the present work is to calculate the Greenhouse Gases emissions inventory in 2006 from a enterprise that produces important inputs for a petroleum industry. The specific purposes were to research the bibliography about the most suitable methodology and its application for this enterprise. The author of this work didnt find any emission factors for CO2 developed in Brazil for calculate the inventory, with a reasonable level of confidence, which can show the real and local situation about this subject. Then, the entire bibliographic search done showed that the works found even in governmental institutions used the IPCC methodology, done by developed countries, that isnt our reality. For this study, it was done several visits to that enterprise and identified all the sources from these GHG, fuel uses and their quantities and intensive bibliographic searches about several national and international methodologies. It was seen the developed work done by this enterprise about generation of seedling (plants) in its market garden. It was chosen the IPCC methodology that was the tool to calculate about 76.000 t of CO2 emitted by the enterprise in 2006. This studied enterprise neutralized 80 t of CO2, through the production of plants cuttings (for donation to people and to plant in around an area that is an environmental passive) in its market garden and what it planted in that passive area in 2006. This was about 0,1% on that it emitted