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An Experimental Analysis in a DICI Engine Powered with MWCNT Blended Emulsions

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Abstract

Owing to the current crisis of environmental degradation generated from various sectors, many efforts have been tried out to commensurate the ecological cycle of the earth. The main contributors causing the environmental degradation are the industrial, transportation, and power plant sectors. Diesel engines are mostly used as a prime mover in those sectors to generate power owing to their superior thermal efficiency. However, at the same time, they also give off deleterious pollutants (like smoke, oxides of nitrogen, unburnt hydrocarbons, etc.). In order to reduce those deleterious pollutants, the present research study is focused to amend the diesel fuel properties on mixing the multi-walled carbon nanotubes (MWCNTs) as fuel-borne additives along with ordinary water methodically. Ordinary water (in prefixed volume percentage, say 2% and 4%) in presence of MWCNT and surfactants was employed to prepare the MWCNT unified water-diesel emulsions methodically and eventually tested for stability. The MWCNT blended water-diesel emulsions were examined in a CI engine to assess the working feature traits. It was established that MWCNT+ water mixture with the diesel, the emissions, and performance traits of the CI engine were ameliorated. It was noted that due to the existence of MWCNT in the water-in-diesel fuels, the secondary atomization effects could have influenced during the combustion period, and thereby caused the reduction in the magnitude of emissions (oxides of nitrogen, unburnt hydrocarbons, and smoke in particular).KeywordsMWCNTEmulsionStabilityPerformanceEmissionsDiesel engine

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The industrial sector accounts for more than 54% of the total energy produced in the world with a predicted annual growth of 1.2%. Currently, most of the industrial sectors use fossil fuels to meet their heat energy requirements and it can be replaced by renewable energy resources particularly solar energy. In this article, an extensive review of various solar thermal energy technologies and their industrial applications are presented. The following industries are covered: power generation, oil and gas, pulp & paper, textile, food processing & beverage, pharmaceutical, leather, automotive, and metal industries. For each of the applications, quality and quantity of heat requirements are identified. Though all the applications are consuming heat in the form of steam/hot water, power plant and enhanced oil recovery have huge potential for solar steam augmentation as compared to other applications. Similarly, applications such as petroleum refining, pulp & paper, and rice mill require a huge amount of steam/hot water. The process heat requirements for textile, food & beverage, pharmaceutical, leather, and automotive industries are at a lower temperature. The integration of solar thermal energy systems with the industrial processes mainly depends on the local solar radiation, availability of land, conventional fuel prices, quality of steam required, and flexibility of system integration with the existing process. Furthermore, challenges involved in the integration of solar thermal energy systems with the process heat industries are explored along with the economics. The future outlook has been proposed to overcome the challenges involved in the integration.
Article
The coconut fatty acid distillate (CFAD) was used as a novel feedstock for biodiesel production in this investigation. Its characterization as fuel in diesel engine was also studied. A maximum biodiesel yield of 92.6% was obtained, when esterification is performed with 10:1 methanol to oil ratio, 2.5% sulphuric acid at 60 °C for 90 min. This is followed by transesterification with optimized parameters of methanol to oil ratio 8:1, 1.5% potassium hydroxide at 60 °C for 90 min. 20%, 40%, 60% and 100% of CFAD biodiesel (CFAB) was added to diesel to form blends CFAB20, CFAB40, CFAB60 and CFAB100. Engine test results showed that the performance of CFAB20 is closer to diesel than the other CFAB blends. The brake thermal efficiency (BTE) of CFAB20 was found to be 4.7% lesser than diesel. Nitrogen oxide emission is higher for all biodiesel blends due to enhanced combustion characteristics. However, carbon monoxide, hydrocarbon and smoke were reduced by 50%, 36.6% and 42.9% respectively for CFAB100 when compared to diesel at full load. Thus it is inferred that the CFAD is a potential source for biodiesel production. CFAB20 can be used in diesel engines with acceptable BTE and reduced emissions without any engine modification.
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As a result of increased global emission, higher fuel price, and limited natural resources, the need of alternative fuels is highly focused by various researchers. Use of edible oil in internal combustion (IC) engine is finding its place to replace the use of conventional fuel. In the present experimental investigation, corn oil methyl ester (COME) and its blends of biodiesel fueled in diesel engine to assess the combustion, performance, emission characteristics. The maximum blend ratio of corn oil methyl ester is limited to 30% with neat diesel. Results showed that using B10 biodiesel blend significantly improved the performance of engine and the maximum engine efficiency using B10 biodiesel blend is found as 33.98% and it is lower than neat diesel. Similarly, the BSFC of diesel engine using B10 biodiesel blend is increased only by 2%, whereas, using B20 and B30, the brake specific fuel consumption (BSFC) increased to about 4 and 6%, respectively. Results showed that the formation of NOx is higher as the oxygen content available in the fuel is higher and similarly, the CO2 during combustion increased. The other emission such as CO and HC are reduced.
Conference Paper
This experimental study, blended jatropha biodiesel and higher alcohol (butanol) were employed in an unmodified diesel engine and its effects on exhaust emissions were studied. The jatropha biodiesel produced from jatropha oil by transesterification process. The evaluated test fuels were diesel (D100), jatropha biodiesel (BD100), 90% of biodiesel and 10% of butanol blend (B90A10), 80% of biodiesel and 20% of butanol blend (B80A20), and 70% of biodiesel and 30% of butanol blend (B70A30). The experimental results were compared with diesel fuel. Results show that the addition of butanol, enhancing emission characteristics owing to its inherent oxygen content. A significant reduction in all emissions was found when adding butanol in biodiesel at all engine loads. Overall, the butanol blending in jatropha biodiesel can be potential alternative fuel owing to its better emission characteristics.
Conference Paper
The Biodiesel is an alternative fuel which can be produced from various feedstocks like vegetable oils, seeds, animal fats and animal tallow. In-case of oil it will be extracted from the seeds with the help of an expelling process. Chemical expelling is efficient method to extract oil from the seeds when compared to mechanical expelling. Due to lower production cost mechanical expelling will be used in most of the cases. This oil consists of FFA content, Based on FFA content single step/two step transterification process will be followed. In this Linseed oil the FFA content is 1.87, hence single step transterification process is followed. The triglyceride esters will be converted into the Mono-glyceride by a catalyzed reaction. The reaction conditions generally involve a trade-off between reaction time and temperature as reaction completeness is the most critical fuel quality parameter. Much of the process complexity originates from contaminants in the feedstock, such as water and free fatty acids, or impurities in the final product, such as methanol, free glycerol, and soap. Processes have been developed to produce biodiesel from high free fatty acid feedstocks, such as recycled restaurant grease, animal fats, and soap stock. This linseed seed has been tested with FTIR analysis, GC-MS analysis and physical properties. All the properties are satisfying the ASTM standards. The physical properties of the linseed biodiesel has been incorporated.
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Liquefied Petroleum Gas (LPG) is a fossil fuel mixture, widely used in domestic and industrial burners for several applications. Non-premixed flames are commonly preferred in these burners owing to their stability and controllability. However, based on operating conditions, non-premixed flames emit emissions such as CO and soot. Several techniques, including supply of coflow air and partial premixing of air with fuel, are used to abate these emissions. Due to multicomponent nature of LPG and its complex oxidation pathway, numerical studies on LPG flames are scarce in literature. However, such studies are helpful in the analysis of flames in several burners. With this motivation, systematic numerical simulations of canonical non-premixed coflow flames of LPG and air, without and with partial premixing of air in the fuel stream, have been presented. A two-dimensional axisymmetric domain is used to represent coflow burner. The numerical model includes sub-models to account for soot formation and its oxidation, and radiation energy loss due to participating species and soot. A short kinetic mechanism with 43 species and 392 elementary reactions is used. Results from the numerical model have been validated for flames of propane, n-butane and LPG. Coflow air is varied as proportions of stoichiometric air. Partial premixing of air to the fuel stream results in a reactant mixture that is not flammable. Characteristics of flames in all these cases are presented systematically using the fields of temperature, flow and species mass fractions. A relative comparison of soot production between all these cases is made. Results reveal that in coflow flames, the net soot emissions increase initially, reach a local maximum and then decrease. In partially premixed flames, soot emissions continuously decrease with an increase in the primary air and become almost negligible after a specified air addition to the fuel stream.
Chapter
Experiments were conducted to determine the engine performance and emission characteristics of Direct Injection (DI)—diesel engine using aqueous cerium oxide nanoparticles (ACONP) and aqueous aluminium oxide nanoparticles (AAONP) as an additive in diesel, ethanol and surfactant blended fuel and were compared with diesel fuel. Blends were prepared by in proportions of Diesel 83%, Ethanol 15% and Surfactant 2% (Span 80) with 50 and 75 ppm aqueous cerium oxide and aqueous aluminium oxide nanoparticles as an additive, denoted as ACONP50, ACONP75, AAONP50 and AAONP75, respectively. The blends are prepared by uniform mixing of nanoparticles with the help of an ultrasonicator. Nanoparticles were acted as an oxygen-donating catalyst which improves the combustion process and results in complete combustion. This will also reduce the hydrocarbons (HC) and carbon monoxide (CO) emissions. It was observed that there is a significant enhancement of performances and decrease of exhaust emissions HC, CO, smoke, slight increase in nitrogen oxides (NOX) as compared to diesel fuel. The combustion parameters like cylinder pressure and heat release rates are increased for both nanoparticles as an additive which has been compared with pure diesel.
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Industry is one of the leading energy consumers with a global share of 37%. Fossil fuels are used to meet more then 80% of this demand. The sun's heat can be exploited in most industrial processes to replace fossil fuels. Integration of a thermal energy storage system is a requisite for sustainability in solar heat for industries. Currently there are only 741 solar heat industrial plants operating with an overall collector area of 662,648 m 2 (567 MW th) that cover very small share of total global capacity. This is only the tip of the iceberg-there is a huge potential that is eager to be exploited. The challenges of increasing cost-effective solar heat applications are development of thermal energy storage systems and materials that can deliver this energy at feasible economic value. Sensible thermal energy storage, which is the oldest and most developed, has recently gained interest due to demand for increased sustainability in energy use. This paper attempts to review these latest trends in sensible thermal energy storage systems and materials that are used in solar industrial applications with a special focus on sustainability. The aim is to provide information for further research and development that shall make solar heat a cost-effective method to meet the increasing energy demand of the industrial sector.
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In this paper, the performance of a gas/oil heat recovery unit is assessed experimentally and by the development of an Aspen model and artificial neural networks. The heat recovery unit is a cross-flow heat exchanger used to recover the residual heat of the exhaust gases coming from a microturbine to drive an absorption chiller. The test facility consists mainly of a microturbine, a heat recovery unit, and an air-cooled absorption chiller. The experiments were conducted at partial power loads and different thermal oil mass flows. Regarding the models, the Aspen model depends on inlet conditions, the mechanical description of the heat recovery unit, and the fluids thermophysical properties, whereas the ANN model consists of 3 trained artificial neurons, 4 inputs (inlet flows and temperatures), and 2 outputs (thermal load and overall heat transfer coefficient). The experimental tests show that the recovery unit recovers from 18.8 kW to 8.1 kW when the microturbine power output is varied from 23 kWe to 4 kWe. Results also show that the overall heat transfer coefficient ranges between 243 W.m−2.K−1 and 89 W.m−2.K−1, while they evidence that the overall heat transfer resistance is controlled by the exhaust gases heat transfer resistance. Furthermore, simulation results show that the Aspen model predicts the heat recovery unit thermal load and overall heat transfer coefficient with average relative differences of 0.93% and 11.27%, respectively, to the experiments. The ANN model evidences average relative differences of 0.51% and 3.48% for the thermal load and overall heat transfer coefficient, respectively.
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Present study investigate the emission pattern of compression ignition engine using Jatropha (J100), Deconal blends with jatropha (JB90D10, JB80D20) and compared with conventional Diesel (D100). Emission parameters such as hydrocarbon (HC), Carbon Monoxide (CO), Nitrogen Oxides (NOx) was measured using gas analyser at various load conditions. Without any additives deconal can be directly added with biodiesel. Engine is quiet smooth in operation and no damage is found in engine parts. Jatropha biodiesel results lower level of carbon monoxide and hydrocarbon with increase in NOx emission. Appending Deconal blends with JB100 shows reduction compared with diesel at all loads.
Article
Solar energy as a plentiful and environment-friendly source of energy has an acceptable potential in nearly most of the regions around the world. Thermal technologies are commonly used to provide heat requirements of different domestic, agricultural, residential, and industrial applications from the sun. This paper reviews thermal performance enhancement techniques of the most widely-used low-temperature solar collectors (LTSCs) including flat-plate collectors (FPCs), evacuated tube collectors (ETCs), and compound parabolic concentrators (CPCs) by introducing challenges and discussing future research potentials. In this regard, energy analysis of each collector type along with the latest advancements to boost the heat collection capability of the LTSCs reported in the previous studies is presented. The discussed methods in this study broadly cover structural modifications, absorber coatings, integration with reflectors, using alternative working fluids including nanofluids, and employing thermal energy storage (TES) systems. This comprehensive review is reflecting the level of technical maturity of each type of LTSCs and is expected to serve scientists, engineers, and developers with the latest achievements in this technology.
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Small Pacific islands are highly dependent on diesel fuel imports to run diesel generators for their electricity needs. Diesel generators are less than 40% efficient and at least 60% of energy is wasted in the form of heat. A significant share of the electricity is consumed for running electric reefer containers that are employed by islanders for the conservation of imported food. This study investigates the feasibility of constructing a Cooling Service Centre (CSC) to host the reefer containers of a small island, utilising the recovered heat from the exhaust of the diesel generators of the island’s power plant, and using Nauru as a case study. Two scenarios are considered: in the first, a cool-store hosting the reefer containers is maintained at a predetermined temperature. In the second, fixed porthole reefer containers are stacked in an open area next to the power plant. In both scenarios, absorption chillers are employed to convert the recovered heat from the generator exhausts and provide cooling. The remainder of the recovered heat is utilised for heating the inlet water of three reverse osmosis (RO) desalination units to increase the flow rate of permeate (fresh water) production. The results show that the most economically feasible scenario is a cool-store held at -20°C, with a pay-back period of 10 years. In a business model where users of the CSC facilities pay for cooling space, the required monthly service charge per reefer container has a maximum of AU$556 for the lowest considered diesel price. This compares favourably with the current monthly electricity cost of AU$1350 that users pay to keep each reefer container running. Such a reduction in the expenses of business owners would make, at least, around a AU$440,000 annual saving in the costs of preservation of imported food and a significant reduction in its market price. Also, the annual water production of desalination units increases by 81 million litres, thus significantly alleviating potential water shortages. Besides, an annual reduction of around 1.1 kilotonnes in total carbon emission is expected to be achieved.
Article
Liquid desiccant dehumidification system driven by heat pump is recognized as an efficient approach for humidity control in the air-conditioning system. The liquid desiccant dehumidification system is optimized by exergy destruction analysis method in the present research. According to the exergy destruction theory, the exergy destruction of a liquid desiccant dehumidification system is divided into exergy destructions arising from heat pump cycle, evaporators, condensers, heat and mass transfer modules and various mixing processes, respectively. The heat and mass transfer process uniformity coefficients γt and γω are proposed to describe the uniformity of the heat and mass transfer driving forces along the whole system. It's indicated γt and γω of the basic cross-flow system are as high as 1.4 and 1.2. Then reducing the exergy destruction is chosen as the guideline to optimize the system. On the basis of the basic cross-flow system, the improved cross-flow system and the improved counter-flow system are further proposed. γt (γω) of the improved systems are reduced to 1.12(1.12) and 1.04(1.01), respectively. Owing to the system optimization, the exergy efficiency increases from 20.1% of the basic cross-flow system to 21% and 25% respectively, COPsys increases from 5.7 to 6.0 and 7.4 respectively. The exergy analysis method is effective for an optimized scenario of a heat-pump driven liquid desiccant process.