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  • Energy Research
  • 12. Responsible consumption
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  • Energy Procedia

  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: Kunio Yoshikawa; Norfadhilah Hamzah; Mohammad Zandi; Koji Tokimatsu;

    Abstract This paper characterized the wood pellet and torrefied wood pellet fuel as compared to coal for 100 MW co-firing power generation plant. There were five experiments to characterise the chemical and physical properties of coal, wood pellet and torrefied wood pellet namely moisture analysis, Thermo gravimetric Analyser (TGA), Bomb Calorimeter, Organic Elemental Analyser and Scanning Electron Microscope (SEM). The moisture analysis result from moisture analyser and TGA shows that the moisture content of torrefied wood pellet is lower than wood pellet at 6.760% and 3.629%. Moreover, the volatile matter, hydrogen and nitrogen content of torrefied wood pellet is lower than wood pellet at 65.20%, 5.993% and 0.4078% correspondingly. The calorific value, fixed carbon content, ash and sulphur also increase in torrefied wood pellet at 20.68 MJ/kg, 28.85%, 2.321% and 0.1656% respectively. In general, torrefaction improve the fuel properties of wood pellet similar to coal. The 100 MW direct co-firing power plant provides less capital investment, operation and maintenance cost for low rate co-firing ratio. However, there is economic challenges for high rate co-firing substation of torrefied wood pellets.

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    Energy Procedia
    Article . 2017 . Peer-reviewed
    License: CC BY NC ND
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    Energy Procedia
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      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Energy Procediaarrow_drop_down
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      Energy Procedia
      Article . 2017 . Peer-reviewed
      License: CC BY NC ND
      Data sources: Crossref
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      Energy Procedia
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    Authors: Nuofu Chen; Han Zhang; Xiulan Zhang; Yiming Bai;

    AbstractEnergy is the biggest crisis to humanity in the future. Nowadays, most of the energy used on earth comes from oil, gas and coal. According to the recent exploring and consuming rates, the energy will be exhausted in 50-100 years. Whether we can solve the crisis is closely related to the survival of humanity on the earth. The irradiation from the sun is the biggest energy source. Building PV power plant to utilize the energy from sun will be an only way to sustain the life cycle on the earth. However, the development of PV power plants require the huge supply of PV cell and the fabrication process may bring a quantity of pollution and waste, which is harmful to the environment. On the other hand, super large PV power plant will occupy huge land. If the land cannot be explored and used reasonably, this will not benefit the human life either. In this article, we address the discussions about the above problems and propose the initial suggestions about development trend of PV industry and the safety operation mode of super PV power plant.

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    Energy Procedia
    Article . 2012 . Peer-reviewed
    License: CC BY NC ND
    Data sources: Crossref
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    Energy Procedia
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      Energy Procedia
      Article . 2012 . Peer-reviewed
      License: CC BY NC ND
      Data sources: Crossref
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      Energy Procedia
      Article
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    Authors: Greg H. Rau; Greg H. Rau;

    AbstractElectrochemical splitting of calcium carbonate (e.g., as contained in inexpensive and abund ant minerals such as limestone) is proposed as a novel method of forming hydroxide solutions that can absorb, neutralize, and store carbon dioxide from the air or from waste streams. CaCO3 is dissolved in the presence of the highly acidic anolyte of a saline water electrolysis cell, forming Ca(OH)2 and H2CO3 (or H2O and CO2). By maintaining a pH between 6 and 9 in the resulting solution, subsequent hydroxide reactions with CO2 primarily produce dissolved calcium bicarbonate, Ca(HCO3)2. Thus, for each mole of CaCO3 split, there can be a net capture of up to 1 mole of CO2. The resulting dissolved Ca(HCO3)2 can be diluted and stored in the ocean, or in reservoirs on land or underground. Net process cost is estimated to be <$100/tonne CO2 mitigated.Other potential co-benefits of the approach include: i) production of significantly carbon-negative H2 if renewable - or nuclear - derived electricity is used as the power source, ii) the option of locally producing electricity and freshwater via fuel cell oxidation of the H2, iii) direct neutralization of ongoing ocean acidification if the Ca(OH)2 generated is added to seawater, iv) preservation or enhancement of otherwise threatened marine shellfish and coral populations, via CO2 absorption and Ca(HCO3)2 formation in or addition to the marine environment, and v) safe ut ilization of the ocean’s vast carbon storage and energy production potentials for CO2 mitigation and “super green” hydrogen generation.

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    Energy Procedia
    Article . 2009 . Peer-reviewed
    License: CC BY NC ND
    Data sources: Crossref
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    Energy Procedia
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      Energy Procedia
      Article . 2009 . Peer-reviewed
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      Energy Procedia
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    Authors: Yano Surya Pradana; Arief Budiman; Wiratni Budhijanto; Hanifrahmawan Sudibyo;

    Abstract Recently, the amount of Yogyakarta province municipal solid waste (MSW) came into Piyungan landfill site stood at around 470 ton/day consisting of 77% organic and 23% inorganic fractions. Annually, there was an increase as many as 8% per annum for the amount of MSW. Reduction of the MSW can be "forced" in integrated waste management site (in Indonesia is called TPST) which was built in the municipal level. In each TPST, there are two main activities which are Recycling and Composting. Both scenarios assume that 23% of inorganic waste can be recycled so that the subsequent need is to manage organic waste. Based on these considerations, calculations performed with: 1). Scenario 1: The TPST has been operated but there is no waste reduction at the source; 2). Scenario 2: TPST is operated and followed by solid waste reduction at the source. If the second scenario is applied, the amount of waste that goes to landfill Piyungan can be reduced up to 200 ton/day. Actually, scenario 1 is the realistic one because of Indonesian’s culture. Unfortunately, as scenario 1 was highly dependent on the TPST, the number of TPST which must be built increase steadily that it can reach 60 units in 2030 which is impossible to find space in Yogyakarta province. If the second scenario is applied, the amount of waste that goes to Piyungan landfill site can be reduced gradually from 25% (1-3 years), 35% (4-7 years), and 50% (8-15 years) through composting activity. The challenge possessed by scenario 2 is how to force people reduce their own organic waste by composting activity.

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    Energy Procedia
    Article . 2017 . Peer-reviewed
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    Energy Procedia
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      Energy Procedia
      Article . 2017 . Peer-reviewed
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      Energy Procedia
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    Authors: Kamel Bennaceur; Kamel Bennaceur; Dolf Gielen;

    AbstractThe International Energy Agency Energy Technologies Perspectives (ETP) model is used for the assessment of the prospects for carbon abatement options, including carbon capture and storage, up to 2050. Three main scenarios are considered: a baseline scenario with current energy policies, an accelerated technology scenario (ACT) with an associated CO2 reduction incentive development, and a scenario in which global greenhouse gas emissions are reduced by 50% compared to current levels in 2050 (BLUE). The analysis suggests that CCS can account for up to 19% of all CO2 reduction in 2050, which would equal 10.4 Gt CO2 capture and storage. The power sector would account for 54% of all CCS, the remainder is in manufacturing industry and the fuel transformation sector.CCS is a critical option. Without CCS, the cost to meet the same target would rise by 71%. The potential rate at which CCS can be introduced exceeds the rate at which regular capital stock is typically replaced, if plants are retrofitted or closed down before the end of their technical life span. Retrofitting of coal plants with CCS plays a very significant role in the ACT Map scenario. But at the price of USD 200/t CO2 envisaged in the BLUE scenario, there is sufficient economic incentive to accelerate the replacement of inefficient power plants with new plants equipped with CCS before the existing plants reach the end of their life span. In the BLUE scenario, 350 GW of coal-fired power-plant capacity is closed down early. The remaining 700 GW consists of 80% new capacity that is equipped with CCS, and 20% retrofits with CCS.Following IEA recommendations, the G8 countries have announced that they will commit 20 demonstration plants for CCS by 2010. Also the G8, China India and Korea have asked the IEA to continue its work on roadmaps and transition paths for CCS in power generation and in industry, in cooperation with other bodies such as CSLF. This work has started and final results will be reported in 2010.

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    Energy Procedia
    Article . 2009 . Peer-reviewed
    License: CC BY NC ND
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    Energy Procedia
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    International Journal of Greenhouse Gas Control
    Article . 2010 . Peer-reviewed
    License: Elsevier TDM
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      Energy Procedia
      Article . 2009 . Peer-reviewed
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      Energy Procedia
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      image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao
      International Journal of Greenhouse Gas Control
      Article . 2010 . Peer-reviewed
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    Authors: Kunio Yoshikawa; Anissa Nurdiawati; Srikandi Novianti; Fumitake Takahashi; +3 Authors

    AbstractThe hydrothermal treatment (HT) has demonstrated the ability to improve fuel characteristics of biomass. On the other hand, the liquid by-product, which potentially contains solubilized nutrient, is being poorly utilized. This paper presents an investigation on HT of empty fruit bunch (EFB) on both solid and liquid product characteristics. In this work, the effects of HT on EFB were investigated at the HT temperatures of 100, 150, 180 and 220°C with the holding time of 30minutes. The results showed that HT can increase the carbon content, remove up to 55% of ash content from EFB, lowering the potassium and chlorine contents down to 0.84% and 0.18%, respectively. Moreover, maximum of 37% of nitrogen, 65% of potassium and less than 10% of phosphorus in EFB were dissolved into the liquid product which positively correlated with the HT temperature. These results demonstrate the possibility of employing HT for producing solid fuel as well as nutrient recovery from EFB.

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    Energy Procedia
    Article . 2015 . Peer-reviewed
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    Energy Procedia
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    http://dx.doi.org/10.1016/j.eg...
    Article . Peer-reviewed
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      Energy Procedia
      Article . 2015 . Peer-reviewed
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      Energy Procedia
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      http://dx.doi.org/10.1016/j.eg...
      Article . Peer-reviewed
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    Authors: Haoran Zhang; Haoran Zhang; Tianqi Xia; Yamin Yan; +6 Authors

    Abstract As a representation of smart and green city development, bike-sharing system is one of the hottest topic in the fields of transportation, public health, urban planning, and so on. With the development of Mobility as a Service (MaaS), emerging technologies such as mobile data mining give some new solutions for optimizing bike-sharing system and predicting the emission reduction. Here, we propose a bike-sharing layout optimization and emission reduction potential analysis structure under the concept of MaaS. A human travel mode detection method and a geometry-based probability model are proposed to support the particle swarm optimization process. We implement a comparison study to analyze the computational efficiency. Taking Setagaya ward, Tokyo as the study case with about 3 million GPS trajectories, the result shows that with the increase of station number from 30 to 90, the adoption of bike-sharing system can reduce about 3.1-3.8 thousand tonnes of CO2 emission.

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    Energy Procedia
    Article . 2018 . Peer-reviewed
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    Energy Procedia
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      Energy Procedia
      Article . 2018 . Peer-reviewed
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      Energy Procedia
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    Authors: Andrew C. Eloka-Eboka; Gillian Ogbene Igbum; Freddie L. Inambao;

    Abstract The urgent need for alternative energy, climate change mitigation and environmental protection in the world today cannot be over-emphasized. Researchers are at top gear in search of non-edible energy crops. The huge environmental benefits of renewable energy notwithstanding, new discoveries in this area arise every day. The potentials of selected tropical seed-oils for biodiesel production and utilization as fuels were therefore explored and subsequently produced. The seed-oils studied include: sand box tree, fluted pumpkin seed and wild melon seeds. Oils of these seeds were extracted, optimized, synthesized and characterized as biodiesel fuels by transesterification process using different alcohol/oil ratios of (4:1 and 6:1) and catalysts types (NaOH and KOH) at optimization temperatures of 38oC and 55oC and reaction time of 5 mins and 30 mins respectively. Optimized biodiesel produced were investigated for their chemo-physical properties in conformity with ASTM standards of biodiesel. Results showed that sandbox tree seeds, wild melon seeds and pumpkin seeds have high percentage oil content (69.32%; 70.24% and 46.88%) respectively. They also hold great potentials as feedstocks in biodiesel production. Chemo-physical properties of the biodiesel produced as well as their blends with automotive gas oil (AGO) fell within specification. Pumpkin seed oil however showed highest average percentage optimized yield of biodiesel (97%) in (1 wt of oil), NaOH catalyst, and alcohol to oil ratio of 6:1 at a reaction temperature of 55°C. Under the given conditions, different biodiesel fuels and blends were successfully produced from the selected feedstock with properties very close to that of conventional AGO. They can therefore be commercialized for large scale utilization as biodiesel fuels or as blends with existing AGO which would be more environmentally friendly.

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    Energy Procedia
    Article . 2017 . Peer-reviewed
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    Energy Procedia
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      Energy Procedia
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    Authors: Longlong Tang; Longlong Tang; Hiromi Kubota; Takahisa Yokoyama; +1 Authors

    AbstractThis study evaluates the potential environmental impacts of deployment of carbon capture and storage (CCS) for pulverized coal power plants in Japan by using LCA, focusing on selected environmental impact categories including global warming. The LIME (Life-cycle impact assessment method based on endpoint modeling) method is used to assess and compare the environmental impacts between three cases, a typical ultra-supercritical pulverized coal-fired power generation system (case 1) and two CCS systems, one comprised of CO2 capture with monoethanolamine (MEA) solvent, compression, seafloor pipeline transportation and below seafloor storage (case 2) and the other case was the same as case 2 except that CO2 transportation by ship was used (case 3). The life cycle GHG emissions for case 1 were 0.89 kg-CO2 (eq.)/kWh. GHG emissions for case 2 and case 3 were 20% and 29%, respectively, of emissions for case 1. However non-GHG emissions increased for case 2 and case 3, especially emissions of NH3 from the CO2 capture process and ethylene oxide from the MEA production process. The results for the 3 cases at the endpoint level, which estimated the damage on four safeguard subjects (human health, social asset, biodiversity and primary production), showed that for case 2 and 3, damage to biodiversity and primary productivity increase by 40% respectively caused by increased feed coal to meet energy consumption on CO2 capture process while the damage to human health decreased by approximately 60% due to the large reduction in CO2 emissions. The increased damage to social assets caused by NH3 emission and increased energy consumption due to CCS is similar with the reduction in damage due to reduction of CO2 emissions.

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    Energy Procedia
    Article . 2014 . Peer-reviewed
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    http://dx.doi.org/10.1016/j.eg...
    Article . Peer-reviewed
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      Energy Procedia
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      http://dx.doi.org/10.1016/j.eg...
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  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: Tsuyoshi Ohishi; Takahiko Endo; Masaki Iijima; Yoshinori Kajiya; +3 Authors

    Abstract(1) It is becoming increasingly evident that the prolonged utilization of fossil fuels for primary energy production, especially coal which is relatively cheap and abundant, is inevitable and that Carbon Capture and Storage (CCS) technology can significantly reduce CO2 emissions from this sector thus allowing the continued environmentally sustainable use of this important energy commodity on a global basis.(2) MHI has co-developed the Kansai Mitsubishi Carbon Dioxide Recovery Process (KM-CDR Process™) and KS-1™ absorbent, which has been deployed in seven CO2 capture plants, now under commercial operation operating at a CO2 capture capacity of 450 metric tons per day (tpd). In addition, a further two commercial plants are now under construction all of which capture CO2 from natural gas fired flue gas boilers and steam reformers. Accordingly this technology is now available for commercial scale CO2 capture for gas boiler and gas turbine application.(3) However before offering commercial CO2 capture plants for coal fired flue gas application, it is necessary to verify the influence of, and develop countermeasures for, related impurities contained in coal fired flue gas. This includes the influence on both the absorbent and the entire system of the CO2 capture plant to achieve high operational reliability and minimize maintenance requirements.(4) Preventing the accumulation of impurities, especially the build up of dust, is very important when treating coal fired flue gas and MHI has undertaken significant work to understand the impact of impurities in order to achieve reliable and stable operating conditions and to efficiently optimize integration between the CO2 capture plant, the coal fired power plant and the flue gas clean up equipment.(5) To achieve this purpose, MHI constructed a 10 tpd CO2 capture demonstration plant at the Matsushima 1000 MW Power Station and confirmed successful, long term demonstration following ∼5000 hours of operation in 2006–07 with 50% financial support by RITE, as a joint program to promote technological development with the private sector, and cooperation from J-POWER.(6) Following successful demonstration testing at Matsushima, additional testing was undertaken in 2008 to examine the impact of entrainment of higher levels of flue gas impurities (primarily SOx and dust by bypassing the existing FGD) and to determine which components of the CO2 recovery process are responsible for the removal of these impurities. Following an additional 1000 demonstration hours, results indicated stable operational performance in relation to the following impurities;(1) SO2: Even at higher SO2 concentrations were almost completely removed from the flue gas before entering the CO2 absorber.(2) Dust: The accumulation of dust in the absorbent was higher, leading to an advanced understanding of the behavior of dust in the CO2 capture plant and the dust removal efficiency of each component within the CO2 recovery system. The data obtained is useful for the design of large-scale units and confirms the operating robustness of the CO2 capture plant accounting for wide fluctuations in impurity concentrations.(7) This important coal fired flue gas testing showed categorically that minimizing the accumulation of large concentrations of impurities, and to suppress dust concentrations below a prescribed level, is important to achieve long-term stable operation and to minimize maintenance work for the CO2 capture plant. To comply with the above requirement, various countermeasures have been developed which include the optimization of the impurity removal technology, flue gas pre treatment and improved optimization with the flue gas desulfurization facility.(8) In case of a commercial scale CO2 capture plant applied for coal fired flue gas, its respective size will be several thousand tpd which represents a considerable scale-up from the 10 tpd demonstration plant. In order to ensure the operational reliability and to accurately confirm the influence and the behavior of the impurities in coal fired flue gas, it is necessary to gain further operational experience with coal fired flue gas at large scale. To this extent, MHI has partnered with Southern Company and the Electric Power Research Institute (EPRI) in the United States for a large scale CCS demonstration project using the KM-CDR Process™ and KS-1™ absorbent. MHI’s coal fired CO2 capture experience and know how at 10 tpd scale aided in the design of the 500 tpd CO2 capture demonstration plant to be deployed at Plant Barry Power Station in Alabama. Commissioning of the plant will take place in Q2 2011 and an extensive test program is planned. Following successful demonstration of this plant, in relation to the effect of scale-up concerning the behavior of impurities, it is envisaged that larger-scale commercial CO2 capture plants can be designed and deployed for the coal fired power sector.(9) This paper will summarize the status of the Matsushima plant operational results and the optimization and examination of impurity removal efficiency within the individual plant components. In addition, the current status of the 500 tpd CO2 capture demonstration plant project will be reported.(10) MHI, as a heavy industrial equipment manufacturer, can provide an integrated plant design through the provision of power generation equipment, flue gas clean up, process plants and CO2 compressors. MHI is actively developing solutions to mitigate global warming through the deployment of economically efficient environmental control technologies and advanced optimization of plant equipment. Related activities such as the large scale demonstration of CO2 capture, with our global partners, are important steps leading to the commercialization of this technology for application in the coal fired power generation sector, thus helping to reduce atmospheric industrial emissions of CO2.

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    Energy Procedia
    Article . 2011 . Peer-reviewed
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      Energy Procedia
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    Authors: Kunio Yoshikawa; Norfadhilah Hamzah; Mohammad Zandi; Koji Tokimatsu;

    Abstract This paper characterized the wood pellet and torrefied wood pellet fuel as compared to coal for 100 MW co-firing power generation plant. There were five experiments to characterise the chemical and physical properties of coal, wood pellet and torrefied wood pellet namely moisture analysis, Thermo gravimetric Analyser (TGA), Bomb Calorimeter, Organic Elemental Analyser and Scanning Electron Microscope (SEM). The moisture analysis result from moisture analyser and TGA shows that the moisture content of torrefied wood pellet is lower than wood pellet at 6.760% and 3.629%. Moreover, the volatile matter, hydrogen and nitrogen content of torrefied wood pellet is lower than wood pellet at 65.20%, 5.993% and 0.4078% correspondingly. The calorific value, fixed carbon content, ash and sulphur also increase in torrefied wood pellet at 20.68 MJ/kg, 28.85%, 2.321% and 0.1656% respectively. In general, torrefaction improve the fuel properties of wood pellet similar to coal. The 100 MW direct co-firing power plant provides less capital investment, operation and maintenance cost for low rate co-firing ratio. However, there is economic challenges for high rate co-firing substation of torrefied wood pellets.

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    Energy Procedia
    Article . 2017 . Peer-reviewed
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    Energy Procedia
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      Energy Procedia
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    Authors: Nuofu Chen; Han Zhang; Xiulan Zhang; Yiming Bai;

    AbstractEnergy is the biggest crisis to humanity in the future. Nowadays, most of the energy used on earth comes from oil, gas and coal. According to the recent exploring and consuming rates, the energy will be exhausted in 50-100 years. Whether we can solve the crisis is closely related to the survival of humanity on the earth. The irradiation from the sun is the biggest energy source. Building PV power plant to utilize the energy from sun will be an only way to sustain the life cycle on the earth. However, the development of PV power plants require the huge supply of PV cell and the fabrication process may bring a quantity of pollution and waste, which is harmful to the environment. On the other hand, super large PV power plant will occupy huge land. If the land cannot be explored and used reasonably, this will not benefit the human life either. In this article, we address the discussions about the above problems and propose the initial suggestions about development trend of PV industry and the safety operation mode of super PV power plant.

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    Energy Procedia
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      Energy Procedia
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    Authors: Greg H. Rau; Greg H. Rau;

    AbstractElectrochemical splitting of calcium carbonate (e.g., as contained in inexpensive and abund ant minerals such as limestone) is proposed as a novel method of forming hydroxide solutions that can absorb, neutralize, and store carbon dioxide from the air or from waste streams. CaCO3 is dissolved in the presence of the highly acidic anolyte of a saline water electrolysis cell, forming Ca(OH)2 and H2CO3 (or H2O and CO2). By maintaining a pH between 6 and 9 in the resulting solution, subsequent hydroxide reactions with CO2 primarily produce dissolved calcium bicarbonate, Ca(HCO3)2. Thus, for each mole of CaCO3 split, there can be a net capture of up to 1 mole of CO2. The resulting dissolved Ca(HCO3)2 can be diluted and stored in the ocean, or in reservoirs on land or underground. Net process cost is estimated to be <$100/tonne CO2 mitigated.Other potential co-benefits of the approach include: i) production of significantly carbon-negative H2 if renewable - or nuclear - derived electricity is used as the power source, ii) the option of locally producing electricity and freshwater via fuel cell oxidation of the H2, iii) direct neutralization of ongoing ocean acidification if the Ca(OH)2 generated is added to seawater, iv) preservation or enhancement of otherwise threatened marine shellfish and coral populations, via CO2 absorption and Ca(HCO3)2 formation in or addition to the marine environment, and v) safe ut ilization of the ocean’s vast carbon storage and energy production potentials for CO2 mitigation and “super green” hydrogen generation.

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    Energy Procedia
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      Energy Procedia
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    Authors: Yano Surya Pradana; Arief Budiman; Wiratni Budhijanto; Hanifrahmawan Sudibyo;

    Abstract Recently, the amount of Yogyakarta province municipal solid waste (MSW) came into Piyungan landfill site stood at around 470 ton/day consisting of 77% organic and 23% inorganic fractions. Annually, there was an increase as many as 8% per annum for the amount of MSW. Reduction of the MSW can be "forced" in integrated waste management site (in Indonesia is called TPST) which was built in the municipal level. In each TPST, there are two main activities which are Recycling and Composting. Both scenarios assume that 23% of inorganic waste can be recycled so that the subsequent need is to manage organic waste. Based on these considerations, calculations performed with: 1). Scenario 1: The TPST has been operated but there is no waste reduction at the source; 2). Scenario 2: TPST is operated and followed by solid waste reduction at the source. If the second scenario is applied, the amount of waste that goes to landfill Piyungan can be reduced up to 200 ton/day. Actually, scenario 1 is the realistic one because of Indonesian’s culture. Unfortunately, as scenario 1 was highly dependent on the TPST, the number of TPST which must be built increase steadily that it can reach 60 units in 2030 which is impossible to find space in Yogyakarta province. If the second scenario is applied, the amount of waste that goes to Piyungan landfill site can be reduced gradually from 25% (1-3 years), 35% (4-7 years), and 50% (8-15 years) through composting activity. The challenge possessed by scenario 2 is how to force people reduce their own organic waste by composting activity.

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    Energy Procedia
    Article . 2017 . Peer-reviewed
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    Energy Procedia
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      Energy Procedia
      Article . 2017 . Peer-reviewed
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      Energy Procedia
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    Authors: Kamel Bennaceur; Kamel Bennaceur; Dolf Gielen;

    AbstractThe International Energy Agency Energy Technologies Perspectives (ETP) model is used for the assessment of the prospects for carbon abatement options, including carbon capture and storage, up to 2050. Three main scenarios are considered: a baseline scenario with current energy policies, an accelerated technology scenario (ACT) with an associated CO2 reduction incentive development, and a scenario in which global greenhouse gas emissions are reduced by 50% compared to current levels in 2050 (BLUE). The analysis suggests that CCS can account for up to 19% of all CO2 reduction in 2050, which would equal 10.4 Gt CO2 capture and storage. The power sector would account for 54% of all CCS, the remainder is in manufacturing industry and the fuel transformation sector.CCS is a critical option. Without CCS, the cost to meet the same target would rise by 71%. The potential rate at which CCS can be introduced exceeds the rate at which regular capital stock is typically replaced, if plants are retrofitted or closed down before the end of their technical life span. Retrofitting of coal plants with CCS plays a very significant role in the ACT Map scenario. But at the price of USD 200/t CO2 envisaged in the BLUE scenario, there is sufficient economic incentive to accelerate the replacement of inefficient power plants with new plants equipped with CCS before the existing plants reach the end of their life span. In the BLUE scenario, 350 GW of coal-fired power-plant capacity is closed down early. The remaining 700 GW consists of 80% new capacity that is equipped with CCS, and 20% retrofits with CCS.Following IEA recommendations, the G8 countries have announced that they will commit 20 demonstration plants for CCS by 2010. Also the G8, China India and Korea have asked the IEA to continue its work on roadmaps and transition paths for CCS in power generation and in industry, in cooperation with other bodies such as CSLF. This work has started and final results will be reported in 2010.

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    Energy Procedia
    Article . 2009 . Peer-reviewed
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    Energy Procedia
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    International Journal of Greenhouse Gas Control
    Article . 2010 . Peer-reviewed
    License: Elsevier TDM
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      Energy Procedia
      Article . 2009 . Peer-reviewed
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      International Journal of Greenhouse Gas Control
      Article . 2010 . Peer-reviewed
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    Authors: Kunio Yoshikawa; Anissa Nurdiawati; Srikandi Novianti; Fumitake Takahashi; +3 Authors

    AbstractThe hydrothermal treatment (HT) has demonstrated the ability to improve fuel characteristics of biomass. On the other hand, the liquid by-product, which potentially contains solubilized nutrient, is being poorly utilized. This paper presents an investigation on HT of empty fruit bunch (EFB) on both solid and liquid product characteristics. In this work, the effects of HT on EFB were investigated at the HT temperatures of 100, 150, 180 and 220°C with the holding time of 30minutes. The results showed that HT can increase the carbon content, remove up to 55% of ash content from EFB, lowering the potassium and chlorine contents down to 0.84% and 0.18%, respectively. Moreover, maximum of 37% of nitrogen, 65% of potassium and less than 10% of phosphorus in EFB were dissolved into the liquid product which positively correlated with the HT temperature. These results demonstrate the possibility of employing HT for producing solid fuel as well as nutrient recovery from EFB.

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    Energy Procedia
    Article . 2015 . Peer-reviewed
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    Energy Procedia
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    http://dx.doi.org/10.1016/j.eg...
    Article . Peer-reviewed
    Data sources: CORE
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      Energy Procedia
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      http://dx.doi.org/10.1016/j.eg...
      Article . Peer-reviewed
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    Authors: Haoran Zhang; Haoran Zhang; Tianqi Xia; Yamin Yan; +6 Authors

    Abstract As a representation of smart and green city development, bike-sharing system is one of the hottest topic in the fields of transportation, public health, urban planning, and so on. With the development of Mobility as a Service (MaaS), emerging technologies such as mobile data mining give some new solutions for optimizing bike-sharing system and predicting the emission reduction. Here, we propose a bike-sharing layout optimization and emission reduction potential analysis structure under the concept of MaaS. A human travel mode detection method and a geometry-based probability model are proposed to support the particle swarm optimization process. We implement a comparison study to analyze the computational efficiency. Taking Setagaya ward, Tokyo as the study case with about 3 million GPS trajectories, the result shows that with the increase of station number from 30 to 90, the adoption of bike-sharing system can reduce about 3.1-3.8 thousand tonnes of CO2 emission.

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    Energy Procedia
    Article . 2018 . Peer-reviewed
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      Energy Procedia
      Article . 2018 . Peer-reviewed
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    Authors: Andrew C. Eloka-Eboka; Gillian Ogbene Igbum; Freddie L. Inambao;

    Abstract The urgent need for alternative energy, climate change mitigation and environmental protection in the world today cannot be over-emphasized. Researchers are at top gear in search of non-edible energy crops. The huge environmental benefits of renewable energy notwithstanding, new discoveries in this area arise every day. The potentials of selected tropical seed-oils for biodiesel production and utilization as fuels were therefore explored and subsequently produced. The seed-oils studied include: sand box tree, fluted pumpkin seed and wild melon seeds. Oils of these seeds were extracted, optimized, synthesized and characterized as biodiesel fuels by transesterification process using different alcohol/oil ratios of (4:1 and 6:1) and catalysts types (NaOH and KOH) at optimization temperatures of 38oC and 55oC and reaction time of 5 mins and 30 mins respectively. Optimized biodiesel produced were investigated for their chemo-physical properties in conformity with ASTM standards of biodiesel. Results showed that sandbox tree seeds, wild melon seeds and pumpkin seeds have high percentage oil content (69.32%; 70.24% and 46.88%) respectively. They also hold great potentials as feedstocks in biodiesel production. Chemo-physical properties of the biodiesel produced as well as their blends with automotive gas oil (AGO) fell within specification. Pumpkin seed oil however showed highest average percentage optimized yield of biodiesel (97%) in (1 wt of oil), NaOH catalyst, and alcohol to oil ratio of 6:1 at a reaction temperature of 55°C. Under the given conditions, different biodiesel fuels and blends were successfully produced from the selected feedstock with properties very close to that of conventional AGO. They can therefore be commercialized for large scale utilization as biodiesel fuels or as blends with existing AGO which would be more environmentally friendly.

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    Energy Procedia
    Article . 2017 . Peer-reviewed
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      Energy Procedia
      Article . 2017 . Peer-reviewed
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    Authors: Longlong Tang; Longlong Tang; Hiromi Kubota; Takahisa Yokoyama; +1 Authors

    AbstractThis study evaluates the potential environmental impacts of deployment of carbon capture and storage (CCS) for pulverized coal power plants in Japan by using LCA, focusing on selected environmental impact categories including global warming. The LIME (Life-cycle impact assessment method based on endpoint modeling) method is used to assess and compare the environmental impacts between three cases, a typical ultra-supercritical pulverized coal-fired power generation system (case 1) and two CCS systems, one comprised of CO2 capture with monoethanolamine (MEA) solvent, compression, seafloor pipeline transportation and below seafloor storage (case 2) and the other case was the same as case 2 except that CO2 transportation by ship was used (case 3). The life cycle GHG emissions for case 1 were 0.89 kg-CO2 (eq.)/kWh. GHG emissions for case 2 and case 3 were 20% and 29%, respectively, of emissions for case 1. However non-GHG emissions increased for case 2 and case 3, especially emissions of NH3 from the CO2 capture process and ethylene oxide from the MEA production process. The results for the 3 cases at the endpoint level, which estimated the damage on four safeguard subjects (human health, social asset, biodiversity and primary production), showed that for case 2 and 3, damage to biodiversity and primary productivity increase by 40% respectively caused by increased feed coal to meet energy consumption on CO2 capture process while the damage to human health decreased by approximately 60% due to the large reduction in CO2 emissions. The increased damage to social assets caused by NH3 emission and increased energy consumption due to CCS is similar with the reduction in damage due to reduction of CO2 emissions.

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    Energy Procedia
    Article . 2014 . Peer-reviewed
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    http://dx.doi.org/10.1016/j.eg...
    Article . Peer-reviewed
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      Energy Procedia
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      http://dx.doi.org/10.1016/j.eg...
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    Authors: Tsuyoshi Ohishi; Takahiko Endo; Masaki Iijima; Yoshinori Kajiya; +3 Authors

    Abstract(1) It is becoming increasingly evident that the prolonged utilization of fossil fuels for primary energy production, especially coal which is relatively cheap and abundant, is inevitable and that Carbon Capture and Storage (CCS) technology can significantly reduce CO2 emissions from this sector thus allowing the continued environmentally sustainable use of this important energy commodity on a global basis.(2) MHI has co-developed the Kansai Mitsubishi Carbon Dioxide Recovery Process (KM-CDR Process™) and KS-1™ absorbent, which has been deployed in seven CO2 capture plants, now under commercial operation operating at a CO2 capture capacity of 450 metric tons per day (tpd). In addition, a further two commercial plants are now under construction all of which capture CO2 from natural gas fired flue gas boilers and steam reformers. Accordingly this technology is now available for commercial scale CO2 capture for gas boiler and gas turbine application.(3) However before offering commercial CO2 capture plants for coal fired flue gas application, it is necessary to verify the influence of, and develop countermeasures for, related impurities contained in coal fired flue gas. This includes the influence on both the absorbent and the entire system of the CO2 capture plant to achieve high operational reliability and minimize maintenance requirements.(4) Preventing the accumulation of impurities, especially the build up of dust, is very important when treating coal fired flue gas and MHI has undertaken significant work to understand the impact of impurities in order to achieve reliable and stable operating conditions and to efficiently optimize integration between the CO2 capture plant, the coal fired power plant and the flue gas clean up equipment.(5) To achieve this purpose, MHI constructed a 10 tpd CO2 capture demonstration plant at the Matsushima 1000 MW Power Station and confirmed successful, long term demonstration following ∼5000 hours of operation in 2006–07 with 50% financial support by RITE, as a joint program to promote technological development with the private sector, and cooperation from J-POWER.(6) Following successful demonstration testing at Matsushima, additional testing was undertaken in 2008 to examine the impact of entrainment of higher levels of flue gas impurities (primarily SOx and dust by bypassing the existing FGD) and to determine which components of the CO2 recovery process are responsible for the removal of these impurities. Following an additional 1000 demonstration hours, results indicated stable operational performance in relation to the following impurities;(1) SO2: Even at higher SO2 concentrations were almost completely removed from the flue gas before entering the CO2 absorber.(2) Dust: The accumulation of dust in the absorbent was higher, leading to an advanced understanding of the behavior of dust in the CO2 capture plant and the dust removal efficiency of each component within the CO2 recovery system. The data obtained is useful for the design of large-scale units and confirms the operating robustness of the CO2 capture plant accounting for wide fluctuations in impurity concentrations.(7) This important coal fired flue gas testing showed categorically that minimizing the accumulation of large concentrations of impurities, and to suppress dust concentrations below a prescribed level, is important to achieve long-term stable operation and to minimize maintenance work for the CO2 capture plant. To comply with the above requirement, various countermeasures have been developed which include the optimization of the impurity removal technology, flue gas pre treatment and improved optimization with the flue gas desulfurization facility.(8) In case of a commercial scale CO2 capture plant applied for coal fired flue gas, its respective size will be several thousand tpd which represents a considerable scale-up from the 10 tpd demonstration plant. In order to ensure the operational reliability and to accurately confirm the influence and the behavior of the impurities in coal fired flue gas, it is necessary to gain further operational experience with coal fired flue gas at large scale. To this extent, MHI has partnered with Southern Company and the Electric Power Research Institute (EPRI) in the United States for a large scale CCS demonstration project using the KM-CDR Process™ and KS-1™ absorbent. MHI’s coal fired CO2 capture experience and know how at 10 tpd scale aided in the design of the 500 tpd CO2 capture demonstration plant to be deployed at Plant Barry Power Station in Alabama. Commissioning of the plant will take place in Q2 2011 and an extensive test program is planned. Following successful demonstration of this plant, in relation to the effect of scale-up concerning the behavior of impurities, it is envisaged that larger-scale commercial CO2 capture plants can be designed and deployed for the coal fired power sector.(9) This paper will summarize the status of the Matsushima plant operational results and the optimization and examination of impurity removal efficiency within the individual plant components. In addition, the current status of the 500 tpd CO2 capture demonstration plant project will be reported.(10) MHI, as a heavy industrial equipment manufacturer, can provide an integrated plant design through the provision of power generation equipment, flue gas clean up, process plants and CO2 compressors. MHI is actively developing solutions to mitigate global warming through the deployment of economically efficient environmental control technologies and advanced optimization of plant equipment. Related activities such as the large scale demonstration of CO2 capture, with our global partners, are important steps leading to the commercialization of this technology for application in the coal fired power generation sector, thus helping to reduce atmospheric industrial emissions of CO2.

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    Energy Procedia
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      Energy Procedia
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