The Role of Atomizing Medium in the Effectiveness of Water-Oil Emulsions to Reduce Unburned Carbon Particles

Author(s):  
Antonio Diego-Marin ◽  
Carlos Melendez-Cervantes ◽  
Alejandro Mani-Gonzalez

Two older boilers were burning low grade heavy fuel oil (number 6) and emitting large amounts of unburned carbon particles. Owing to the short life remaining of the units and economic constrains, it was not possible to change to a better fuel or install new burners. To contribute to the solution of this problem, an experimental program was carried out by emulsifying water in the fuel oil. Tests were performed in a scale furnace (0.35MWth) and the emulsions that produced the best results were assessed in the two boilers, 28 and 34 MWe capacity with Y-jet atomizer type. The system to prepare the emulsion was very simple: water was added into the oil before the fuel oil pump, no chemical products were added and a static mixed was used to improve the water size distribution, which 90% ranged from 1 to 9 micron. In the pilot furnace the emulsions were prepared with 5 and 10% water and atomized with compressed air. Particle reductions of 43 and 67% were obtained compared with the net heavy fuel oil. In the boilers, the emulsions were prepared with the same amount of water, and were atomized with saturated steam. In the 28 MWe boiler, a similar particle reduction was obtained to that of the scale furnace. However, in the 34 MWe boiler there was no particle abatement. By using a commercial fluid dynamic computer code, it was found that the combustion air transferred heat to the steam raising its temperature. Thus, in the mixing chamber of the Y-jet atomizers, the steam was superheated and destroyed the water droplets of the emulsion. Compressed air and saturated steam as atomizing medium of the emulsions had similar effect on the unburned particle reduction. However, the effectiveness of the emulsions may be affected by the steam. Care should be taken to avoid the use of steam with a temperature higher than the saturated water temperature.

Author(s):  
Antonio Diego-Marin ◽  
Carlos Melendez-Cervantes ◽  
Armando Giles-Alarcon

A study was carried out to find out the cause of premature plugging of air heaters of a 350 MWe oil fired boiler. The unit burnt a heavy fuel oil number 6, with both high levels of sulfur (3.75%) and asphaltenes (16.2%), as well as high viscosity (555 SSF at 50°C) and API gravity of 11.2. Particle concentration at the furnace exit and at the stack were measured, also flue gas analyses were performed at the same sites. In the furnace were employed water cooled probes of six meters in length which allowed traversing 70% of its width. In addition, the oil droplet size distribution from an atomizer was measured with a Malver Particle Sizer. Cold condition using simulating fluids were taken in this analysis. Also, the unburned carbon particles size distribution, both from the furnace exit and from the stack, was performed with a particle Malver Sizer. The atomizer produced large oil drops, 5.7% by volume larger than 300 micron size, which were considered as promoters of unburned carbon. The concentration of carbon particles in the stack was 60% of that of the furnace exit. Furthermore, the particles from the stack were of smaller size (95% <150 μm) than those of the furnace (89% <150 μm). Deposition of carbon particles in the internal component of the boiler, mainly in the air heaters, was the cause of this finding. To solve the premature plugging of the air heaters of this oil fired boiler, the atomizers should be modified to reduce at a minimum level the oil drops larger than 200 micron size.


Author(s):  
Antonio Diego-Marin ◽  
Carlos Melendez-Cervantes ◽  
Angel Alberto Mendez Aranda ◽  
Armando Giles-Alarcon

Reduction of both atomizing steam and particulate emissions were investigated in a 350 MWe utility boiler. A residual fuel oil was dispersed as a fine mist into the furnace with sixteen atomizers of internal turbulent chamber type. The existing atomizers were replaced by Y-jet type atomizers. To do this, full scale prototypes were designed and tested in a cold model rig using mineral oil as the fuel and compressed air as the atomizing medium. The oil droplet size distribution was measured from a single port of each prototype by using a Malvern particle sizer. The prototype to be tested in the power station was selected based on the smallest oil droplets produced along with lower compressed air consumption. In the power station, the burners were modified to install the new design of Y-jet atomizers. Field tests were conducted at 50, 75 and 100% load. Atomizing steam was measured, as well as particulate emissions and the furnace exist flue gas temperature. With the Y-jet atomizers, the atomizing steam was reduced 55% with respect to the original atomizers; the unburned carbon particles were reduced by a maximum of 50%, the furnace exit gas temperature was similar between the two type of atomizers and no side effects were observed in the boiler.


Author(s):  
M Coelho ◽  
F Nash ◽  
D Linsell ◽  
J. P. Barciela

The contribution of cogeneration plants to a reduction in primary energy consumption will be important not only in lowering emissions to the atmosphere but also in cutting production costs by increasing the overall efficiency of fuel conversion to the electricity and heat used by process industries. This paper demonstrates the importance of the interactions of the utility needs of a process with the development and design of a cogeneration system to maximize fuel efficiency and achieve environmental compliance for a chemical plant. The cogeneration system in this project is based on a diesel cycle engine burning heavy fuel oil (HFO), driving an alternator and with an exhaust gas heat recovery boiler supplementary fired with either HFO or natural gas. The normal operation of the cogeneration plant is with the engine running at 95–100 per cent maximum continuous rating (MCR) with the supplementary firing of the boiler modulating to meet the process requirements for saturated steam at 10 barg. In addition to recovering waste heat from the engine exhaust gas (EEG), supplementary firing using the excess oxygen in the exhaust gas enables the process steam required by the plant to be produced without the loss of energy involved in heating combustion air. At the same time the reduced volume of oxygen available to the flame reduces peak temperature and NOx emissions, this being further enhanced by the phased combustion design of the burner. The technology demonstrated in this application is generally as used in gas turbine cogeneration cycles burning natural gas. The use of HFO in this instance necessitated the use of a reciprocating engine driven generator and the development of supplementary firing of the exhaust gases. The successful development of the technology enables this reciprocating engine based cogeneration system to be scaled up or, possibly more importantly, down utilizing HFO, natural gas or renewable derived liquid or gaseous fuels. Its implementation using spark ignition engine generators retrofitted to economic boilers may be one way general industry in the United Kingdom might meet its climate change levy (CCL) targets for energy reduction and help approach the government's carbon reduction requirements.


The changing pattern of demand for oil products has required that refining practices be adjusted to maximize yields of premium products from crudes. There has been a concomitant deterioration in the quality of the ‘residual’ or ‘heavy’ fuel oil used in power generation. A major constraint on the burning of such heavy fuel is a restriction on particulate emissions. These emissions largely comprise carbon particles (coke), which form from the individual oil spray droplets and remain unburnt. Poorer quality oils have an increased propensity to form coke, and can give rise to unacceptable emissions. One way of countering these increases is to make the fuel spray finer and hence improve burn-out. Research has been aimed firstly at quantifying the effects of those oil properties that directly influence coke formation and combustion and then at developing improved atomizers and water-in-oil emulsions to reduce droplet sizes.


2021 ◽  
Vol 18 (6) ◽  
pp. 108-117
Author(s):  
A. V. Dmitrenko ◽  
M. A. Kolosova

The development of stationary energy seems to be an important aspect of introduction of energy-saving technologies in transportation sector. In Russia, it is conditioned by the main provisions of the Energy Strategy of the Russian Federation until 2030. In this regard, the problem of efficient use of low-grade heat based on the organic Rankine cycle (ORC) in stationary heat energy supply units in the transport industry is urgent. In particular, this task is typical for boiler houses converted from heavy fuel oil to gas fuel. In this case, the efficiency of ORC application will primarily be determined by the efficiency of the used heat exchangers (HE) with a phase transition, as a result of which, both technically and theoretically, the problem of designing and calculating the optimal characteristics of these HE will be of great interest.The article presents a theoretical and computational model of heat transfer during phase transitions in turbulent flows based on the relations obtained by the stochastic theory of hydrodynamics and heat transfer. The modelling of the effect of turbulence during the phase transition with undeveloped boiling of the bubble mode is considered. The comparison results show satisfactory conformity of the values obtained according to the formula based on stochastic equations with the values calculated according to the empirical formula for the flow in a pipe, used in the engineering method of designing heat exchangers. The results obtained open the prospect for studying the processes of heat transfer during phase transitions in turbulent flows of HE to reduce their overall and mass characteristics, as well as to increase the energy efficiency of both the devices themselves and the efficiency of the entire energy complex.


Author(s):  
Laís A. Nascimento ◽  
Marilda N. Carvalho ◽  
Mohand Benachour ◽  
Valdemir A. Santos ◽  
Leonie A. Sarubbo ◽  
...  

2017 ◽  
Vol 68 ◽  
pp. 203-215 ◽  
Author(s):  
Dionisis Stefanitsis ◽  
Ilias Malgarinos ◽  
George Strotos ◽  
Nikolaos Nikolopoulos ◽  
Emmanouil Kakaras ◽  
...  

1996 ◽  
Vol 26 (2) ◽  
pp. 2241-2250 ◽  
Author(s):  
M.A. Byrnes ◽  
E.A. Foumeny ◽  
T. Mahmud ◽  
A.S.A.K. Sharifah ◽  
T. Abbas ◽  
...  

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