Steam, its generation and use.

Vols. for <41st.ed.-> accompanied by CD-ROM version.

Otimização do Funcionamento de Caldeiras Aquatubulares em Indústria de Processo Químico

O presente trabalho centrou-se na otimização do rendimento térmico de duas caldeiras aquatubulares da empresa RAR- Refinaria de Açúcar Reunidas, com a finalidade de identificar onde ocorrem perdas de energia e, desta forma, propor soluções para a sua minimização. Para tal, realizaram-se ensaios em duas caldeiras da empresa providas de queimadores mistos, ou seja podem operar com fuelóleo e gás natural, tanto individualmente, como simultaneamente, sendo que para a realização dos ensaios apenas se utilizou o fuelóleo devido ao seu menor custo. Na caldeira designada por 1 realizaram-se ensaios para os caudais de 300, 500, 800, 1000, 1200, 1400 e 1600 kg/h de fuelóleo. A gama de rendimentos térmicos obtida foi entre 88,3 e 91,2%. Na caldeira designada por 3, efetuaram-se ensaios para os caudais de fuelóleo de 300, 500, 700, 900, 1000, 1200, 1400, 1500 e 1800 kg/h e os rendimentos térmicos obtidos foram entre 85,2 e 88,0%. Em ambas as caldeiras e para caudais baixos verificou-se que a quantidade de ar introduzida no processo de combustão era superior à necessária, conduzindo a uma diminuição dos valores de rendimento térmico. Para 500 kg/h de fuelóleo, por exemplo, a quantidade de ar utilizada foi cerca de duas vezes superiores ao valor estequiométrico. Tendo em conta estes factos, foi proposto ao gestor de energia a implementação de uma nova relação de ar/combustível vs caudal de combustível no sistema de controlo das referidas caldeiras. Após alguns testes (excluindo 300 kg/h de fuelóleo devido a questões de operação), considerou-se como caudal mínimo de operação os 500 Kg/h de fuelóleo nas respetivas caldeiras 1 e 3. Verificou-se que os rendimentos térmicos aumentaram, no caso da caldeira 1, para valores entre os 90,1 e 91,3% e, na caldeira 3, para valores entre 89,0 e 90,9%. Por fim, efetuou-se uma breve análise económica com o intuito de se avaliar e quantificar o que a empresa pode poupar com esta medida. O lucro anual pode oscilar entre 14.400 e 62.640€ ou 104.400 e 136.800€, para as caldeiras 1 e 3, respetivamente.

Fuel switching

The present Master dissertation is a project whose main objective is to identify value creation opportunities through fuel switching in the Portuguese industry, services, agriculture and fishing sectors. Fuel switching opportunities are characterized by type of fuel transition, type of technology transition, economy subsectors prone to have fuel switching and value created through fuel shift. Results suggest tomato concentrate, dairy, beer manufacturing and sugar refining subsectors is where prevalence of fuel oil steam boilers is high, for such cases conversion to natural gas steam boilers should result in operations having a ratio of NPV over CAPEX larger than ten and a payback period just under one year. Results further suggest food, beverages, textile, chemicals and wood subsectors currently operate between ten and twenty cogeneration Diesel engines that can be either modified to operate with natural gas or replaced by new natural gas cogeneration systems. Financial modeling indicates that both options have great value creation potential. The current analysis aims to be used by natural gas suppliers and energy project promoters to identify new potential deals as well as by heavy energy consumers to mitigate their energy related costs.

Projecte d'instal·lació de caldera de vapor de 5.000 kg/h i serveis auxiliars per [a] una empresa situada a Vic

L’empresa RUSCALLEDA, S.L., ubicada a la localitat de Vic, es dedica a l’elaboració de productes alimentaris. La instal·lació actual de generació de calor utilitza una caldera antiga de combustible líquid i té una capacitat de producció de vapor de 1.500 kg/h. A causa de la demanda creixent de productes semielaborats, l'empresa vol instal·lar tres unitats noves de la línia final de productes semielaborats. Aquestes noves unitats tindrien un considerable consum d’energia calorífica en forma de vapor i requeririen actualitzar la instal·lació actual de producció i distribució de calor. L’objecte del projecte és la instal·lació d’un segon generador de vapor que sigui capaç d’alimentar la instal·lació actual més l’ampliació, quedant el generador actual en paral·lel per ser utilitzat en cas d’emergència

British manufactures.

[Vols. 4-6] are called "Series IV-VI."

The Elements of mining engineering [microform] /

Includes indexes.

Illustrated technical dictionary in six languages, English, German, French, Russian, Italian, Spanish /

Vols. 7-13 have added t.p.: Schlomann-Oldenbourgh illustrierte technische wörterbücher, unter mitwirkung hervorragender fachieute des in- und auslandes, hrsg. von Alfred Schlomann ... Müchen und Berlin, Druck und verlag von R. Oldenbourg; London, Constable & Co., etc.

Boiler inspector's manual & engineer's handbook of safe boiler operation ...

Various pagings.

Boiler Safety Act, and boiler rules and regulations /

Description based on: 1972 ed.; title from cover.

The first to make boiler plates in America : Lukens Iron and Steel Company.

Mode of access: Internet.

Fuel economy in boiler rooms; a development of Fuel economy and CO₂ recorders, published in the engineers' study course from Power.

First edition, 1914, has title: Fuel economy and CO₂ recorders.

La vapeur, sa production et son emploi,

Mode of access: Internet.

Scientific water correction.

Mode of access: Internet.

Chemistry of potassium halides and their role in corrosion in biomass and waste firing

Compared to the use of traditional fossil fuels (coal, oil, natural gas), combustion of biomass and waste fuels has several environmental and economic advantages for heat and power generation. However, biomass and waste fuels might contain halogens (Cl, Br, F), alkali metals (Na, K) and heavy metals (Zn, Pb), which may cause harmful emissions and corrosion problems. Hightemperature corrosion occurs typically on furnace waterwalls and superheaters. The corrosion of the boiler tube materials limits the increase of thermal efficiency of steam boilers and leads to costly shutdowns and repairs. In recent years, some concerns have been raised about halogen (Cl, Br, and F)-related hightemperature corrosion in biomass- and waste-fired boilers. Chlorine-related high-temperature corrosion has been studied extensively. The presence of alkali chlorides in the deposits is believed to play a major role in the corrosion observed in biomass and waste fired boilers. However, there is much less information found in literature on the corrosion effect of bromine and fluorine. According to the literature, bromine is only assumed to play a role similar to chlorine; the role of fluorine is even less understood. In this work, a series of bubbling fluidized bed (BFB) bench-scale tests were carried out to characterize the formation and sulfation behaviors of KCl and KBr in BFB combustion conditions. Furthermore, a series of laboratory tests were carried out to investigate the hightemperature corrosion behaviors of three different superheater steels (10CrMo9-10, AISI 347 and Sanicro 28) exposed to potassium halides in ambient air and wet air (containing 30% H2O). The influence of H2O and O2 on the high-temperature corrosion of steels both with and without a salt (KCl) in three gas atmospheres (2% H2O-30% O2-N2, 2% H2O-2% O2-N2 and 30% H2O-2% O2-N2) was also studied. From the bench-scale BFB combustion tests, it was found that HBr has a clearly higher affinity for the available K forming KBr than HCl forming KCl. The tests also indicated that KCl has a higher tendency for sulfation than KBr. From the laboratory corrosion tests in ambient air (also called “dry air” in Paper III and Paper IV), it was found that at relatively low temperatures (≤ 550 °C) the corrosivity of KBr and KF are similar to KCl. At 600 °C, KF showed much stronger corrosivity than KBr and KCl, especially for 10CrMo9-10 and AISI 347. When exposed to KBr or KF, 10CrMo9-10 was durable at least up to 450 °C, while AISI 347 and Sanicro 28 were durable at least up to 550 °C. From the laboratory corrosion tests in wet air (30% H2O), no obvious effect of water vapor was detected at 450 °C. At 550 °C, the influence of water vapor became significant in some cases, but the trend was not consistent. At 550 °C, after exposure with KBr, 10CrMo9-10 suffered from extreme corrosion; after exposure with KF and KCl, the corrosion was less severe, but still high. At 550 °C, local deep pitting corrosion occurred on AISI 347 and Sanicro 28 after exposure with KF. Some formation of K2CrO4 was observed in the oxide layer. At 550 °C, AISI 347 and Sanicro 28 suffered from low corrosion (oxide layer thickness of < 10 μm) after exposure with KBr and KCl. No formation of K2CrO4 was observed. Internal oxidation occurred in the cases of AISI 347 with KBr and KCl. From the laboratory corrosion tests in three different gas atmospheres (2% H2O-30% O2-N2, 2% H2O-2% O2-N2 and 30% H2O-2% O2-N2), it was found that in tests with no salt, no corrosion occurred on AISI 347 and Sanicro 28 up to 600 °C in both the “O2-rich” (2% H2O-30% O2-N2) and “H2O-rich” (30% H2O-2% O2-N2) gas atmospheres; only 10CrMo9-10 showed increased corrosion with increasing temperature. For 10CrMo9-10 in the “O2-rich” atmosphere, the presence of KCl significantly increased the corrosion compared to the “no salt” cases. For 10CrMo9-10 in the “H2O-rich” atmosphere, the presence or absence of KCl did not show any big influence on corrosion. The formation of K2CrO4 was observed only in the case with the “O2-rich” atmosphere. Considering both the results from the BFB tests and the laboratory corrosion tests, if fuels containing Br were to be combusted, the corrosion damage of superheaters would be expected to be higher than if the fuels contain only Cl. Information generated from these studies can be used to help the boiler manufacturers in selecting materials for the most demanding combustion systems.

Alternativas de uso da borra de café através de hidrólise ácida, enzimática, ou como substrato para a produção das enzimas: lacase e celulase

In the industrial production of soluble coffee, huge amounts of extracted coffee residues are generated; onaverage, for eachtonne of green coffee extracted, 480 kg of coffee ground waste is produced. This is a solid residue currently used to generate energy at the steam boilers from the soluble coffee industry. Some is also used or as fertilizer on agriculture fields. Seeking a better end use, the work reported here aimed to study the viability of hydrolyzing the coffee ground residue for the production of carbohydrates. Hydrolysis was undertaken with hydrochloric acid at different temperatures and pressures, using a water bath or autoclave.An enzymatic hydrolysis with Viscozyme Lwas developed using Whatman filter paper No1 and the optimal conditions were determined using a rotational central composite experimental design (DCCR).The best conditions to hydrolyze filter paper cellulose were 50 FBG (Fungal β-glucanase) of Viscozyme L at pH 4.0 for 1.0 h and 45 ºC. The ground coffee was hydrolyzed under the same conditions as described above for filter paper, however this enzymatic hydrolysis was not efficient. A combination of enzymatic hydrolysis as a pre-treatment for the ground coffee followed by acid hydrolysis using HCl conducted in an autoclave (120 C for 2.0 h) resulted in higher production of glucose as analyzed by HPLC. Another end use of the ground coffee evaluated was as source of substrate in the culture medium to grow Botryosphaeria rhodina MAMB-05 to produce the enzymes laccase and cellulase. Highest enzyme titres obtained were with 8% (w/v) coffee grounds to which was added a minimum salts medium(Vogel), under agitation conditions (180 rpm) at 28ºC. The phenolic compounds present in the coffee grounds appear to have induced laccase by Botryosphaeria rhodina.