Juan Daniel Martínez

Production of activated carbon by waste tire thermochemical degradation with CO2

The thermochemical degradation of waste tires in a CO(2) atmosphere without previous treatment of devolatilization (pyrolysis) in order to obtain activated carbons with good textural properties such as surface area and porosity was studied. The operating variables studied were CO(2) flow rate (50 and 150 mL/min), temperature (800 and 900 degrees C) and reaction time (1, 1.5, 2, 2.5 and 3h). Results show a considerable effect of the temperature and the reaction time in the porosity development. Kinetic measurements showed that the reactions involved in the thermochemical degradation of waste tire with CO(2), are similar to those developed in the pyrolysis process carried out under N(2) atmosphere and temperatures below 760 degrees C, for particles sizes of 500 microm and heating rate of 5 degrees C/min. For temperatures higher than 760 degrees C the CO(2) starts to oxidize the remaining carbon black. Activated carbon with a 414-m(2)/g surface area at 900 degrees C of temperature, 150 mL/min of CO(2) volumetric flow and 180 min of reaction time was obtained. In this work it is considering the no reactivity of CO(2) for devolatilization of the tires (up to 760 degrees C), and also the partial oxidation of residual char at high temperature for activation (>760 degrees C). It is confirmed that there are two consecutive stages (devolatilization and activation) developed from the same process.

Catalytic pyrolysis of wood biomass in an auger reactor using calcium-based catalysts

Wood catalytic pyrolysis using calcium-based materials was studied in an auger reactor at 450°C. Two different catalysts, CaO and CaO·MgO were evaluated and upgraded bio-oils were obtained in both cases. Whilst acidity and oxygen content remarkable decrease, both pH and calorific value increase with respect to the non-catalytic test. Upgrading process was linked to the fact that calcium-based materials could not only fix the CO2-like compounds but also promoted the dehydration reactions. In addition, process simulation demonstrated that the addition of these catalysts, especially CaO, could favour the energetic integration since a lowest circulation of heat carrier between combustor and auger reactor should be needed. An energy self-sustained system was obtained where thermal energy required for biomass drying and for pyrolysis reaction was supplied by non-condensable gas and char combustion, respectively.

Demonstration of the waste tire pyrolysis process on pilot scale in a continuous auger reactor.

This work shows the technical feasibility for valorizing waste tires by pyrolysis using a pilot scale facility with a nominal capacity of 150 kWth. A continuous auger reactor was operated to perform thirteen independent experiments that conducted to the processing of more than 500 kg of shredded waste tires in 100 h of operation. The reaction temperature was 550°C and the pressure was 1 bar in all the runs. Under these conditions, yields to solid, liquid and gas were 40.5 ± 0.3, 42.6 ± 0.1 and 16.9 ± 0.3 wt.% respectively. Ultimate and proximate analyses as well as heating value analysis were conducted for both the solid and liquid fraction. pH, water content, total acid number (TAN), viscosity and density were also assessed for the liquid and compared to the specifications of marine fuels (standard ISO 8217). Gas chromatography was used to calculate the composition of the gaseous fraction. It was observed that all these properties remained practically invariable along the experiments without any significant technical problem. In addition, the reaction enthalpy necessary to perform the waste tire pyrolysis process (907.1 ± 40.0 kJ/kg) was determined from the combustion and formation enthalpies of waste tire and conversion products. Finally, a mass balance closure was performed showing an excellent reliability of the data obtained from the experimental campaign.

Carbonyl emission and toxicity profile of diesel blends with an animal-fat biodiesel and a tire pyrolysis liquid fuel.

In this paper, two diesel fuels, an animal-fat biodiesel and two diesel blends with the animal-fat biodiesel (50vol.%) and with a tire pyrolysis liquid (TPL) fuel (5vol.%) have been tested in a 4-cylinder, 4-stroke, turbocharged, intercooled, 2.0L Nissan diesel automotive engine (model M1D) with common-rail injection system and diesel oxidation catalyst (DOC). Carbonyl emissions have been analyzed both before and after DOC and specific reactivity of carbonyl profile has been calculated. Carbonyl sampling was carried out by means of a heated line, trapping the gas in 2,4-DNPH cartridges. The eluted content was then analyzed in an HPLC system, with UV-VIS detection. Results showed, on the one hand, an increase in carbonyl emissions with the biodiesel fraction in the fuel. On the other hand, the addition of TPL to diesel also increased carbonyl emissions. These trends were occasionally different if the emissions were studied after the DOC, as it seems to be selectivity during the oxidation process. The specific reactivity was also studied, finding a decrease with the oxygen content within the fuel molecule, although the equivalent ozone emissions slightly increased with the oxygen content. Finally, the emissions toxicity was also studied, comparing them to different parameters defined by different organizations. Depending on the point of study, emissions were above or below the established limits, although acrolein exceeded them as it has the least permissive values.

Dominant macular colobomata

Hereditary bilateral macular colobomata are not a consequence of an anomalous closure of the fetal fissure. Their extreme rarity, their lack of embryological explanation, and their morphologic similarity to postinflammatory congenital macular scars called the hereditary-malformative etiology of this entity in question. The authors describe a four generation family with seven affected members with isolated autosomal dominant bilateral macular colobomata.

E proteins sharpen neurogenesis by modulating proneural bHLH transcription factors’ activity in an E-box-dependent manner

Class II HLH proteins heterodimerize with class I HLH/E proteins to regulate transcription. Here, we show that E proteins sharpen neurogenesis by adjusting the neurogenic strength of the distinct proneural proteins. We find that inhibiting BMP signaling or its target ID2 in the chick embryo spinal cord, impairs the neuronal production from progenitors expressing ATOH1/ASCL1, but less severely that from progenitors expressing NEUROG1/2/PTF1a. We show this context-dependent response to result from the differential modulation of proneural proteins’ activity by E proteins. E proteins synergize with proneural proteins when acting on CAGSTG motifs, thereby facilitating the activity of ASCL1/ATOH1 which preferentially bind to such motifs. Conversely, E proteins restrict the neurogenic strength of NEUROG1/2 by directly inhibiting their preferential binding to CADATG motifs. Since we find this mechanism to be conserved in corticogenesis, we propose this differential co-operation of E proteins with proneural proteins as a novel though general feature of their mechanism of action.

E proteins differentially co-operate with proneural bHLH transcription factors to sharpen neurogenesis

Basic HLH proteins heterodimerize with class I HLH/E proteins to promote transcription. Here we show that E proteins differentially co-operate with proneural bHLH transcription factors sharpening their neurogeneic activity. We find that inhibiting BMP signaling or its target ID2, in the chick embryo spinal cord, impairs the neuronal production from progenitors expressing ATOH1/ASCL1, but less severely that from progenitors expressing NEUROG1/2/PTF1a. We define the mechanisms of this differential response as a dual co-operation of E proteins with proneural proteins. E proteins synergize with bHLH proteins when acting on CAGSTG motifs, thereby facilitating the neurogenic activity of ASCL1/ATOH1 which preferentially bind to such motifs. Conversely, E proteins restrict the strong neurogenic potential of NEUROG1/2 by directly inhibiting their preferential binding to CADATG motifs. Since we find this mechanism to be conserved in corticogenesis, we propose this dual co-operation of E proteins with bHLH proteins as a novel though general feature of their mechanism of action.

Power Generation Alternatives From Biomass Gasification Using Different Syngas Pathways

In this work three different ways to produce 1 MWe from biomass gasification syngas are presented. The studied pathways considered the biomass gasification in order to produce syngas able to be transformed into liquid fuels through (i) fermentation and (ii) Fischer Tropsch (FT) synthesis. Later, both liquid fuels were assumed to be powered in a spark ignition engine and in a compression ignition engine, respectively. The third pathway is (iii) the direct use of syngas in a gas-fired reciprocating engine. Syngas composition was predicted from three residual lignocellulosic biomasses (rice husk, sugarcane bagasse and coffee husk) using a stoichiometric equilibrium model. It was found that the direct use of syngas (LHV ~6.72 MJ/Nm 3 ) needs less biomass (~800 kg/h) to achieve 1 MWe in comparison with the other two pathways. Diesel fuel from FT and ethanol from the fermentation process require around 1500 kg/h and 2500 kg/h of biomass respectively to achieve the same power. The FT synthesis considered the production of a synthetic liquid fuel similar to diesel fuel in terms of heating value (LHV ~44 MJ/kg), while syngas fermentation took into account the ethanol production (LHV ~27 MJ/kg). The above results, for the three different fuels, were assessed considering the thermal efficiencies of each specific internal combustion engine.