Nuevo registro de Govenia purpusii (Orchidaceae) en el Parque Nacional La Malinche, Tlaxcala

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Antecedentes y Objetivos: Govenia purpusii es una especie de la familia Orchidaceae, tiene una distribución restringida dentro de los bosques subalpinos de los estados de Chiapas, Colima, Durango, Guerrero, Hidalgo, Jalisco, México, Michoacán, Oaxaca, Puebla, Querétaro, Veracruz y Zacatecas. El propósito de este trabajo fue describir el hallazgo de esta especie presente en el Parque Nacional La Malinche, Tlaxcala, para incluirla en el inventario florístico. Métodos: Se identificó una población de G. purpusii en campo y se realizaron colectas. A través del cotejo de material botánico recolectado con ejemplares de herbario, se determinó la especie considerando caracteres vegetativos y florales para su identificación. Resultados clave: La especie se encontró en una vegetación de Quercus-Pinus a 2780 m de altitud; comparte el espacio con Selaginella sp., Oxalis sp., Peperomia sp. y Pinguicula moranensis. Conclusiones: Se recomienda monitorear esta población debido a la reducida área de distribución dentro del Parque Nacional La Malinche y al escaso conocimiento sobre orquídeas terrestres en la entidad. La extinción local representaría una pérdida de material genético para la especie. No se debe interpretar este registro como una ampliación reciente de área de distribución; la presencia dentro de esta zona puede ser el resultado de la fragmentación de los bosques en la Faja Neovolcánica Transmexicana.

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The whimsical nature of the fuel causes a constant disturbance to the uidised bed and thus to the equipment that relies on the output of the uidised bed. A control system must suppress the uctuations in the output of the uidised to secure the optimal operation of the equipment downstream. In order to do so successfully, a thorough understanding of the dynamics of the thermal conversion of particles is necessary. That is the subject of this thesis. The thermal conversion of solid particles usually occurs in an apparatus where many particles convert simultaneously. The total gas or heat production of all particles together constitutes the behaviour of the system. If there are enough particles, it is not necessary to account for the behaviour of every individual particle to predict the behaviour of the system as a whole. Due to the large amount of particles, it is su??cient to know the averaged behaviour over all particles. One may directly derive equations for this average that do not depend on the individual particles in the system. This can be done using a population balance equation. This equation describes the expected distribution of particles over space and over the relevant particle properties. Suppose the gas or heat production of a single particle is known as a function of the particle properties and the external condition (e.g. temperature). In that case the total gas or heat production in the apparatus can be calculated by integrating that function, weighted with the expected particle distribution. There are thus two main issues to be resolved in order to model the dynamics of a system in which particles are converted under the in uence of heat: 1. The behaviour in time of a single particle must be expressed as a function of the relevant particle properties and the external conditions. 2. The population balance equation must be established and solved to calculate the expected particle distribution. Both issues are addressed in this thesis. The population balance is subsequently used in a model of a circulating uidised gasi??er. The ??nal chapter of this thesis concerns the problem of tar in biomass gasi??cation. The thermal conversion of a single particle consists of several processes: drying, pyrolysis, gasi??cation and combustion. There exist good descriptions of the single particle behaviour for gasi??cation and combustion. There is no good solution for the behaviour of particle during drying and pyrolysis yet. Therefore, pyrolysis is studied in this thesis. Drying is discussed when the results of experiments are presented. New method to measure reactivity To study the behaviour of biomass particles under uidised bed conditions, a new measurement method has been developed. The method consists of a heated uidised bed placed on a balance. A batch of biomass particles is dropped into the bed. The mass decrease of these particles in the bed can be monitored using the balance. Nitrogen is used as uidising medium, so that the pyrolysis process can be observed without subsequent combustion or gasi??cation of the particles. The uidised bed causes large weight uctuations on the balance. Therefore signal processing is necessary to extract the mass decrease of the biomass particles from the signal. Two types of signal processing have been tested: a linear and a non-linear ??lter. The linear ??lter is a low-pass ??lter that attempts to separate the high frequency uidised bed noise from the low frequency mass decrease of the biomass. This ??lter exploits the fact that one knows that the mass decrease must be much slower than the weight uctuations due to the uidised bed. The non-linear ??lter is a wavelet ??lter with thresholding. This ??lter exploits the fact that one expects the mass decrease to be much smoother than the uidised bed noise. The noise can then be estimated and subtracted from the signal. The wavelet thresholding ??lter proves to be more successful for two reasons: ??rstly the ??ltered signal is smoother and leads to more reproducible results (especially of the pyrolysis time) and secondly the method allows for a more concise statement of the assumptions and approximations involved. The measurement results show that the pyrolysis time depends almost linearly on the particle diameter. This leads to the conclusion that the activation energy of the pyrolysis reaction must be relatively low, and thus lower than is usually assumed. The measurements also showed that the pyrolysis time may depend linearly on moisture content. This suggests that drying is determined solely by the external heating rate. However, the measurements also leave room for the interpretation that the presence of moisture leads to a more or less constant increase in pyrolysis time. This suggests that pyrolysis will start before drying is complete. The measurements are inconclusive in this respect and further research into drying is recommended. Pyrolysis model A physical and mathematical model of biomass pyrolysis has been developed to determine which particle properties are essential to the pyrolysis behaviour of a single particle. The development starts with a derivation of the equations that are generally used to describe biomass pyrolysis. The derivation shows which assumptions are implied by the equations that are commonly used. One of the most important assumptions is that the pyrolysis reaction rate depends linearly on the concentration of fresh biomass. It is in fact more likely that the reaction rate depends linearly on the internal surface area of fresh biomass. The implied assumption is therefore that the internal surface area depends linearly on the biomass concentration. This assumption is hardly justi??ed. An investigation of the biomass structure and of the actual reaction order is recommended. It is also shown that there are two groups of kinetic parameters to be found in literature. Between these groups the proposed activation energy of the pyrolysis reaction di??ers by a factor two (approximately). The groups di??er in the way in which the kinetic parameters are determined. Fitting of the kinetic parameters using a model that incorporates heat transfer and the pyrolysis reaction leads to the lower activation energy while TGA measurements lead to a higher activation energy. It is shown in this thesis that the lower activation energy leads to better results. The TGA experiments rely on the assumption that the external heat transfer to the samples was not rate limiting during the experiments. This assumption can, however, only be veri??ed if the reaction kinetics are already known. If the reaction kinetics are derived from TGA experiments under the false assumption that external heat transfer is not rate limiting, then the activation energy will be overestimated. A simpli??ed analytical solution to the pyrolysis equations has been derived in this thesis. This solution is shown to describe the experiments quite well. The main particle properties that determine its pyrolysis behaviour are found to be: particle diameter, type of fuel, initial moisture content and the initial density Population balance The nature and the derivation of the population balance equations are discussed in detail. The analytical solution for the population balance equation is obtained, but is found to be of little use for anyone who wants to understand the behaviour of the system in which the particles are converted under the in uence of heat. Therefore, the population balance equation is rewritten in terms of moments of the particle properties. Examples of these moments are average diameter, variance of diameter etc. This led to signi??cant insight in the behaviour of a CFB gasi??er. The main conclusion is that average particle size is insu??cient to characterise the speed at which the gasi??er responds. The variance of particle size is very important too. If the particle distribution of e.g. size is broader, the gasi??er will respond to changes with a larger uctuation in gas production and gas quality. At the same time it will recuperate slower. Changes of average particle size in the feed lead naturally to a broader particle distribution. The e??ect of changes in particle size is much larger than the e??ect of changes in moisture content. Gasi??er model The population balance is applied in a model for a CFB biomass gasi??er. This model is designed in such a way that it will be straightforward to incorporate new insights and results in areas where the present research has not focused, such as tar conversion, char gasi??cation and drying. Simulations with the model show that the particle size has a much more profound e??ect on the gasi??er than the fuel moisture content.

  • Research Article
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A STUDY ON THE PROPERTIES OF THE 12 MAY WENCHUAN EARTHQUAKE-INDUCED DEBRIS FLOW
  • Jan 1, 2011
  • Yingjie Han + 6 more

Debris flows triggered by earthquakes are recognized globally for their huge destructive power. Studies on the development features of debris flow are essential for disaster prevention and mitigation and the results can be used as a scientific basis for assuring public security, preventing debris-flow disasters and reconstructing the afflicted areas by earthquake. Taking the, Niujuan Gully, as the case study area, this paper discusses field observations of the initiation and path of debris flows in the epicentral area of the 12 May, 2008 Wenchuan Earthquake. Based on the natural conditions and debris flow distribution in the study area, a field control network was established to monitor the gully bed, typical slopes and channel sections of different kinds of debris flows that initiated from hillslopes and gullies. We observed debris flows and their change under different rainfall circumstances, surveyed slope, section, channel and gully bed by means of GPS, GPT-3002 total-station instrument and 3D laser scanning system and drew digital topographic maps, sectional maps and profile maps with a 1:50 scale. Based on the observed data, we probed into the erosion laws and development features(including erosion, transportation, deposition, etc) of different kinds of debris flows and analyzed debris flow discharge, erosion-deposition variation and destructive magnitude. The findings provided data support for debris flow risk assessment and monitoring systems.

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The CMS Detector Power System
  • Jan 1, 2008
  • S Lusin

The power system for the on-detector electronics of the CMS Experiment comprises approximately 12000 low voltage channels, with a total power requirement of 1.1 MVA. The radiation environment inside the CMS experimental cavern combined with an ambient magnetic field (reaching up to 1.3 kGauss at the detector periphery) severely limit the available choices of low voltage supplies, effectively ruling out the use of commercial off-the-shelf DC power supplies. Typical current requirements at the CMS detector front end range from 1A-30A per channel at voltages ranging between 1.25V and 8V. This requires in turn that the final stage of the low voltage power supply be located on the detector periphery. Power to the CMS front-end electronics is stabilized by a 2 MVA uninterruptible power supply (UPS) located in a CMS surface building. This UPS isolates the CMS detector from disturbances on the local power grid and provides for 2 minutes of autonomy following a power failure, allowing for an orderly shutdown of detector electronics and controls. This paper describes the design of the CMS Detector Power System, reviews the process of its installation and commissioning, and discusses issues of power distribution common to current-generation collider detectors. I. OVERVIEW OF THE CMS DETECTOR CMS is a general-purpose detector at the LHC accelerator at the CERN laboratory in Geneva, Switzerland. A description of this detector is beyond the scope of this paper, but may be found in reference [1]. A. Requirements of CMS Detector The front-end electronics of the CMS detector has 12090 low-voltage channels, requiring 1182 KVA of power. The steel yoke structure of the CMS detector serves as a flux return for the 4-Tesla solenoid inside the detector structure. Since the magnetic field of the solenoid is large enough to drive sections of this steel yoke into saturation there is an ambient magnetic field that can reach up to 1.3 KG outside detector in the regions where low voltage power supplies are mounted. Typical commercial low-voltage power supplies are not designed for operation in a magnetic field and many have been noted to fail destructively at fields above 150 Gauss. In addition, the high radiation environment inside the CMS experimental cavern imposes constraints on the design of low voltage supplies from the standpoint of semiconductor displacement damage and single-event effects. Together, these constraints rule out the use of general-purpose commercial power supplies. Typical front-end current requirements are 1 to 30A per channel, at voltages from 1.25 to 8.0V. Since cable power dissipation must be kept within reasonable limits, the placement of the final power supply stage is constrained to be within ~10m of the front-end electronics, that is, on the detector periphery. B. CMS power distribution requirements The power cable paths between CMS on-detector systems and the power distribution area in the adjacent equipment cavern are typically 100 to 140m in length. Power to the detector is supplied at 380 and 230 VAC (three-phase) and at 385 VDC. No neutral is distributed. The CMS detector power system serves all of the low voltage power needs on the detector from a single distribution network. Although there are other power distribution networks at the CMS site, there are no persistent connections between the CMS detector and any of these other networks. This single-source powering scheme enables a unified earthing structure for the CMS detector and simplifies considerations of detector response to disturbances in power distribution. C. CMS power distribution system architecture The detector power system is powered by a 2 MVA uninterruptible power supply (UPS) installed on the surface. The UPS provides for at least 2 minutes autonomy in the event of a power failure. This length of time is sufficient to provide for an orderly shutdown of subdetector power systems. The UPS powers a bank of 6 isolation transformers located underground in one of the CMS caverns. The transformers are apportioned by subdetector and geographical detector region. Each transformer feeds one or more power distribution cabinets containing circuit breakers, monitoring equipment and programmable logic controllers. Power from an individual circuit breaker channel can be turned on and off via a remote control system, but in the event of a fault condition the circuit breaker must be reset manually. This is a deliberate design choice to prevent casual responses to fault conditions. The isolation transformers consist of four 230V and two 380V three-phase units, each containing an interwinding electrostatic screen. Static compensators are connected to selected distribution cabinets in order to provide power factor correction (PFC) for certain subdetectors (Fig 1.)

  • Research Article
  • 10.22067/geo.v6i4.63302
شبیهسازی اثر تغییر اقلیم بر جابهجایی زمانی تاریخ وقوع اولین و آخرین یخبندانهای پاییزه و بهارۀ ایران
  • Jan 21, 2018
  • محمد دارائی + 3 more

هدف از پژوهش کنونی بررسی دورنمایی از اثرات احتمالی تغییر اقلیم بر جابه‌جایی زمانی تاریخ وقوع اولین و آخرین یخبندان‌های پاییزه و بهارۀ ایران است. بدین منظور از داده‌های دیده‌بانی 43 ایستگاه همدید کشور (1981-2010) و داده‌های شبیه‌سازی شدۀ LARS WG در دو مدل آب‌وهوای جهانی GFCM21 و HadCM3 در بازه‌های زمانی (2065-2046) و (2099-2080)، تحت سه سناریوی انتشار A1B، A2 و B1استفاده گردید. نتایج، بیانگر جابه‌جایی اولین یخبندان پاییزه‌ به سمت اوایل زمستان و جابه‌جایی آخرین یخبندان بهاره به‌سوی اواخر زمستان در گسترۀ ایران است. پراکنش زمانی-مکانی تغییرات متفاوت است؛ به‌گونه‌ای که بیشترین جابه‌جایی‌های مثبت در رخداد اولین یخبندان پاییزه در دورۀ (2065-2046) در ایستگاه‌هایی چون خرم‌‌آباد، رشت و گرگان مشاهده می‌شود. میزان تغییرات در ایستگاه‌های شمال شرقی (سبزوار و سمنان)، نیمۀ جنوبی (کرمان، بم و آباده) و بیشتر ایستگاه‌های شمال‌غرب نسبت به دیگر مناطق کمتر است. در دورۀ (2080-2099) بیشترین روند منفی در ایستگاه‌های گرگان، رشت، اردبیل و شهرکرد خواهد بود. خوی، قزوین، بم و کاشان کمترین جابه‌جایی منفی خواهند داشت.

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