The Effect of Spent Coffee Grounds to the Growth of Solanum lycopersicum (Tomato)

Six billion tonnes of spent coffee grounds (SCG) are thrown untreated into landfills, leading the spent coffee grounds to leach organic pollutants that may potentially harm bodies of water and emit methane, a greenhouse gas, into the atmosphere. Studies have confirmed that the ratio of carbon and nitrogen (C: N) of SCG is ideal for plant fertilizers. This study focused on determining the effects of SCG on the growth of tomato plants using four parameters: the number of leaves, the average leaf surface area, and the relative growth rate. The study used an experimental research design to study the causal relationship between SCG treatments and plant growth. Tomato seeds were grouped into four and sown on separate pots. The study used three trials, each containing different weights of SCG, namely: 0 g, 5 g, 9 g, and 14 g. The SCG treatments were applied after germination using the side-dressing method. The number of expanded leaves, leaf surface area, and relative growth rate of the tomato plants were observed every five days for 45 days. The researchers found that SCG treatments that exceeded SCG-5 displayed adverse effects on the growth of the tomato. Thus, the relative growth rate and SCG treatments of over 5 g are inversely related to one another. Results show that SCG-5 had the highest positive effect on plant growth in terms of all the parameters. The researchers can then conclude that SCG-5 is an effective alternative fertilizer that improves plant growth

The Inclusiveness and Emptiness of <i>Gong Qi</i>: A Non-Anglophone Perspective on Ethics from a Sino-Japanese Corporation

This article introduces a non-Anglophone concept of gong qi(communal vessel, 公器) as a metaphor for ‘corporation’. It contributes an endogenous perspective from a Sino-Japanese organizational context that enriches mainstream business ethics literature, otherwise heavily reliant on Western traditions. We translate the multi-layered meanings of gong qi based on analysis of its ideograms, its references into classical philosophies, and contemporary application in this Japanese multinational corporation in China. Gong qi contributes a perspective that sees a corporation as an inclusive and virtuous social entity, and also addresses the elusive, implicit, and forever evolving nature of organizational life that is rarely noticed. We propose gong qi can be applied in other organizations and wider cultural contexts to show a new way of seeing and understanding business ethics and organization. Rather than considering virtue as a list of definable individual qualities, we suggest that the metaphor of gong qi reveals how virtue can be experienced as indeterminate, yet immanently present, like the substance of emptiness. This, then allows us to see the virtue of immanence, the beauty of implicitness, and hence, the efficacy of gong qi

Biomass gasification and catalytic conversion of synthesis gas:characterisation of cobalt catalysts for Fischer-Tropsch synthesis

Abstract Biomass gasification as a thermochemical treatment method is typically used for heat and power production. Instead of burning the producer gas, it can be converted to added-value products, i.e to fuels and chemicals. One such conversion is the catalytic Fischer-Tropsch synthesis (FTS) which converts synthesis gas to a chain of aliphatic hydrocarbons (FT diesel) as studied in this thesis. This requires, however, proper cleaning steps of producer gas, such as the removal of tar compounds and other impurities. These cleaning steps are not considered in this thesis. The first goal of the thesis was to determine the tar content in the producer gas from a small scale biomass gasifier. This subject is discussed in Paper I. The second and main goal of the thesis was the preparation and characterization of cobalt (or iron) catalysts for catalytic conversion of a gas mixture close to the synthesis as discussed in Papers II-V. The overall aim of the second part was to study the effects of promoters on the reducibility of cobalt and the effects of different calcination conditions on the degree of reduction and size of the metallic cobalt particles. In this later part different catalytic supports were used. According to the results of the thesis, naphthalene and toluene were the main tar compounds in the producer gas representing almost 80 % of the GC detected tar compounds. Only traces of polycyclic aromatic compounds were detected and no phenolic compounds were found in the gas. Further, a number of supported heterogeneous catalysts for FTS using cobalt (Co) or in some cases iron (Fe) as the active metal were prepared and characterized. These catalysts were supported on alumina (Al2O3), titanium dioxide (TiO2) or silicon carbide (SiC). Catalysts were promoted with Ru, Re or Rh in the concentrations of 0, 0.2, 0.5, and 1.0 mass-%. Several characterization methods (such as H2-TPR, catalytic activity measurements, N2 physisorption, CO chemisorption, X-ray photoelectron spectroscopy (XPS), and X-ray diffraction (XRD)) were used to find answers to the behaviour of these catalysts under selected conditions and in the model reaction of FTS. Based on the results, there are significant differences in the characteristics of the catalysts, the differences are dependent of the supports used, promoters added and calcination conditions used. The properties of the support, especially the pore size distribution will effect the distribution of products formed in the Fischer-Tropsch synthesis. Addition of promoters and variatons in calcination conditions will effect the dispersion and the particle size of the active metal.Tiivistelmä Biomassan kaasutus on termokemiallinen prosessi, jota käytetään pääosin sähkön- ja lämmöntuotannossa. Polton sijaan kaasutuksessa muodostuva synteesikaasu voidaan puhdistaa ja hyödyntää edelleen katalyyttisesti polttoaineiden ja kemikaalien valmistuksessa. Eräs mahdollisuus synteesikaasun hyödyntämiseen on Fischer-Tropsch synteesi (FTS), jossa koboltti- tai rautakatayyteillä voidaan tuottaa alifaattisia hiilivetyketjuja (FT-dieseliä), mitä on tutkittu tässä työssä. FT-synteesi vaatii kuitenkin puhtaan tuotekaasun ja sen vuoksi tervayhdisteet ja muut epäpuhtaudet on poistettava kaasusta. Kaasun puhdistusta ei ole kuitenkaan tutkittu tässä työssä. Työn ensimmäisenä tavoitteena oli määrittää biomassan kaasutuksessa käytettävän pienikokoisen myötävirtakaasuttimen kaasun koostumus ja tervayhdisteet ja niiden pitoisuudet (julkaisu I). Toisena, ja tämän työn päätavoitteena oli Fischer-Tropsch -synteesissä käytettävien koboltti- ja rautakatalyyttien valmistus ja karakterisointi sekä käyttö synteesikaasun katalyyttisessä konvertoinnissa (julkaisut II-V). Erityisesti tutkittiin promoottorimetallien ja kalsinointiolosuhteiden vaikutusta koboltin pelkistymiseen ja kobolttimetallipartikkelien kokoon. Lisäksi tutkittiin ja vertailtiin erilaisia tukiaineita. Työn tulosten perusteella naftaleiini ja tolueeni olivat pääasialliset tervayhdisteet myötävirtakaasuttimen tuotekaasussa ja niiden osuus oli yli 80 % kaasukromatografisesti havaittavista tervayhdisteistä. Lisäksi havaittiin pieniä määriä polysyklisiä aromaattisia yhdisteitä, kun taas fenolisia yhdisteitä ei havaittu tuotekaasussa. Työssä valmistettiin ja karakterisoitiin lukuisa määrä erilaisia FT-katalyyttejä, joissa aktiivisena metallina oli koboltti tai rauta. Katalyyteissä tukiaineena oli alumiinioksidi (Al2O3), titaanidioksidi (TiO2) tai piikarbidi (SiC) ja promoottorimetallina joko Ru, Re tai Rh (pitoisuudet 0, 0.2 tai 1.0 massa-%). Katalyyttien karakterisointiin käytettiin useita menetelmiä, kuten H2-TPR, N2-adsorptio, CO-kemisorptio, XPS, XRD ja lisäksi määritettiin katalyyttien aktiivisuus ja selektiivisyys valituissa olosuhteissa FT-synteesin mallireaktioissa. Tulosten perusteella katalyyttien välillä havaittiin selkeitä eroja riippuen käytetystä tukiaineesta, promoottorista ja kalsinointiolosuhteista. Tukiaineen ominaisuudet, erityisesti huokoskokojakauma vaikuttavat FT-synteesin tuotejakaumaan. Promoottorien lisäys katalyyttiin sekä kalsinointiolosuhteet vaikuttavat lisäksi dispersioon ja aktiivisen metallien partikkelikokoon

Catalytic effect of transition metals (copper, iron, and nickel) on the foaming and properties of sugar-based carbon foams

Abstract Recently, bio-based carbon foams have gained much interest in many chemical industry fields because of their unique structure and properties. This study provides new information on the effects of catalytic metals (iron, nickel, and copper) on the foaming process. Specifically, the effects of these catalysts on the density, foam growth, and cell size and then further on the pore size distribution and specific surface areas after the physical activation are considered. Furthermore, some of the activated sugar foams were used in adsorption tests using methylene blue as adsorbent. Results showed that the highest effect on foam density was obtained using the iron catalyst in the foaming process. In addition, increasing the iron amount, the development of micro-pores decreased from 95.2 to 60.3% after cabonization and activation of the foams. Nickel and iron had the highest and lowest effect on foam rise at 1375 and 500%, respectively. Interestingly, when the nickel catalyst was used, cell sizes and surface areas two times larger than those when the foams were prepared with the iron and copper catalysts was obtained. The specific surface area of activated sugar-based carbon foams changed significantly with the increased copper amount inside the foaming solution in compared with iron or nickel catalyst. Methylene blue adsorption capacity of additional series of activated sugar foams decreased from 28 to 9% when meso-pore amount decreased

Physical activation of wooden chips and the effect of particle size, initial humidity, and acetic acid extraction on the properties of activated carbons

Abstract In this research study, two different wooden biomasses (birch and pine) were thermally carbonized and steam-activated into activated carbons in a one-stage process. The effects of particle size and humidity (as received and oven-dried) on the properties, such as specific surface areas, pore volumes, and pore size distributions, of the final activated carbon characteristics were examined. Another set of biomasses (birch, spruce, and pine) was pre-treated before carbonization and the activation steps through an extractive process using a weak acetic acid in Soxhlet extractors. According to the results, the dried samples had a slightly lower surface area, while no difference was observed in the yields. For the extracted samples, there was a significant difference, especially in the pore size distributions, compared to the non-extracted samples. There appeared to be a shift from a meso-microporous distribution to a microporous distribution caused by the extractive pre-treatment

Effect of some process parameters on the main properties of activated carbon produced from peat in a lab-scale process

Abstract Activated carbons (ACs) are widely used in different industrial processes as adsorbents for pollutant removal or as catalytic material support. The parameters and methods of activation can vary, and they affect the final characteristics of ACs, e.g., specific surface area, pore size distribution, and surface functional groups. The results of this study show that microporosity and mesoporosity can be modified, variating these parameters. ACs from Northern Finland Region peat have been prepared through physical activation with steam. The process has been evaluated using the design of experiment approach. Different parameters have been considered as factors, including holding time, oven temperature, heating rate, steam flow, nitrogen flow, kiln rotation, and biomass initial mass. Based on these factors, several responses characterizing the porosity and the elemental analysis of ACs have been selected. All the data collected have been processed statistically using the Fractional Factorial Resolution IV design linear model in a screening configuration fitted with a partial least squares regression using MODDE 9.1 by Umetrics Software

Effect of calcination conditions on the dispersion of cobalt Over Re, Ru and Rh promoted Co/γ-Al₂O₃ catalysts

Abstract The effects of catalyst calcination conditions, such as calcination temperature and calcination atmosphere composition on the dispersion of cobalt particles over Co/γ-Al₂O₃ catalysts for Fischer–Tropsch conversion of synthesis gas are studied. A number of catalysts were prepared by incipient wetness impregnation of 20-wt% of cobalt onto γ-Al₂O₃ and promoted with 0.5 wt% ruthenium, rhenium, and rhodium. Metal dispersions of active metals were studied by chemisorption of carbon monoxide. The highest dispersion for Co/γ-Al₂O₃ catalyst was achieved by calcination at 400 °C in a flow of N₂. Co metal dispersion seem to be increased in the calcination steps if a flowing gas was used instead of static calcination conditions. The addition of promoter metals like Ru, Re or Rh enhances the dispersion of the active metal