The alkali solution consisting of 5% NaOH, 5% NaCl, 2% Tea is most suitable for making pidan. During the soaking period, the values of pH increased from pH 9.02~ 9.19 to pH 12 in the egg white and increased from PH 6.1 to PH 11.63 in the egg yolk. Quail's egg jelled on the 7th day of immersion and the hen's egg and duck's egg jelled on the 10th day of immersion. The Quail's egg ripened at $25^{\circ}C$ in 30~35 days, and Sunghua crystals were formed at the end of the ripening period The moisture content of pidans decreased by 3.5~4.0%, but relatively crude protein, crude fat and crude ash increased by 1.0%, 1.9% and twice respectively. The content of Ca in the hen's pidan and quail's pidan increased about 40%, that of K in the duck's pidan increased about 13% and that of Mg in the hen's pidan and duck's pidan increased about 23~28%. The content of Na in the 3 groups all increased approximately 7 times. The content of total cholesterol level in pidan yolks decreased by 21~40% in each pidan. As a result of a sensory evaluation, the white hen's pidan was most agreeable in flavor and the quail's pidan was most agreeable.
The mechanism of a matrix modification for the trace determination of volatile lead and bismuth by an electro-thermal atomic absorption spectrophotometry was studied by a X-ray diffractometry (XRD). For the investigation of structures, the ash products of the elements were produced by using a palladium as a matrix modifier with or without aluminum or nickel as an auxiliary modifier. The same charring conditions as in the analysis of samples were applied together with much concentrated solution of analytical elements and modifiers in a graphite furnace to get a large amount of the product for XRD. The XRD patterns showed PbPd3 for lead and BiPd3 for bismuth. These mean that the reaction procedures through the charring and atomization were changed from $Pb^{2+}$${\rightarrow}$ PbO ${\rightarrow}$$Pb^0$ to $Pb^{2+}$${\rightarrow}$ PbO ${\rightarrow}PbPd_3$${\rightarrow}$ Pb o for lead and from $Bi^{3+}$${\rightarrow}$ BiO ${\rightarrow}$ Bi o to $Bi^{3+}$${\rightarrow}$ BiO ${\rightarrow}$$BiPd_3$${\rightarrow}$$Bi^0$ for bismuth by the addition of modifiers. The volatile elements were stabilized by the formation of palladium alloys through a charring process. Charring temperatures were raised about 500 $^{\circ}C$ by the alloying and the atomization was also stabilized for the enhancement of sensitivities.
Today, concrete remains the most important, durable, and reliable material that has been used in the construction sector, making it the most commonly used material after water. However, cement continues to exert many negative effects on the environment, including the production of carbon dioxide (CO2), which pollutes the atmosphere. Cement production is costly, and it also consumes energy and natural non- renewable resources, which are critical for sustainability. These factors represent the motivation for researchers to examine the various alternatives that can reduce the effects on the environment, natural resources, and energy consumption and enhance the mechanical properties of concrete. Geopolymer is one alternative that has been investigated; this can be produced using aluminosilicate materials such as low calcium (class F) FA, Ultra-Fine GGBS, and high calcium FA (class C, which are available worldwide as industrial, agricultural byproducts.). It has a high percentage of silica and alumina, which react with alkaline solution (activators). Aluminosilicate gel, which forms as a result of this reaction, is an effective binding material for the concrete. This paper presents an up-to-date review regarding the important engineering properties of geopolymer formed by FA and slag binders; the findings demonstrate that this type of geopolymer could be an adequate alternative to ordinary Portland cement (OPC). Due to the significant positive mechanical properties of slag-FA geopolymer cements and their positive effects on the environment, it represents a material that could potentially be used in the construction industry.
Proceedings of the Korean Institute of Building Construction Conference
/
2021.05a
/
pp.225-226
/
2021
Recently, environmental problems have emerged as a major issue all over the world due to an increase in carbon dioxide(CO2). The amount of CO2 generated during cement production accounts for 6% to 8% of domestic CO2 emissions and a solution to reduce CO2 emissions the construction industry is trying to use mineral admixtures to reduce cement. Since digestion has no firing process the advantage of it is that there is no air pollution to occur. In this study, we studied the compressive strength of binary non-cement mortar containing rice husk powder extracted from digestion by the ratio of 10%, 20%, 30%, 40%. As a result, the table flow was increased when the mixing rate of rice husk powder extracted from digestion was higher, and the highest compressive strength was shown when the rice husk powder extracted from digestion mixing rate was 10%.
Ha, Ji-Won;Yi, Kwang Bok;Lee, Si Hyun;Rhee, Young-Woo;Kim, Jong-Nam
Korean Chemical Engineering Research
/
v.46
no.2
/
pp.423-429
/
2008
Currently, Ash-free clean coal producing process by solvent extraction is under development. The produced ash-free clean coal can be directly combusted in a gas turbine which results in substantial improvement of power generation efficiency. However, the clean coal produced by the solvent extraction still contain trace amount of alkali metal which may cause corrosion on turbine blades during the direct combustion. In present work ${\alpha},{\beta}$-metal (Zr and Ti) phosphates and H-Y zeolite were synthesized and their ion exchange characterizations were investigated for the application on alkali metal removal for clean coal production. $Na^+$ ion removal capacities of the metal phosphates and H-Y zeolite were measured and compared in both aqueous solution (100 ppmw, $Na^+$) and coal dissolved N-methyl-2-pyrrolidone (NMP, 12 ppmw $Na^+$) at elevated temperature. In aqueous solution, the ${\beta}$ form metal phosphates showed very high ion exchange capacities compared to ${\alpha}$ form. ${\beta}$ form metal phosphates also showed higher $Na^+$ removal capacities than H-Y zeolite. In ion exchange medium of NMP, all the ${\alpha}$ form metal phosphates showed over 90% of $Na^+$ ion removal efficiency in the temperature range of 200 to 400 while that of H-Y zeolite decreased as a half when the temperature was over 350. In addition, the regenerated metal phosphates by acid treatment showed no sign of degradation in $Na^+$ removal efficiency. Among the metal phosphates used, $Zr_{0.75}Ti_{0.25}(HPO_4)_2$ showed the best performance in $Na^+$ removal and is expected to be the most suitable inorganic ion exchanger for the alkali metal removal process.
Physicochemical properties of safflower sprouts grown in there different lights red, blue, and white; control exposed to limited light and subjested to different drying processes were investigated. Moisture contents of safflower sprouts grown different lights and treated with hot dry air were as follows: 9.38%(white light), 5.70%(blue light), 12.21%(red light), and 7.84%(control; no light). The moisture contents of freeze-dried safflower sprouts were as follow as: 9.95%(white light), 11.30%(blue light), 11.25%(red light), and 10.45%(control). Crude ash contents of the hot air-dried sprouts were as follows: 4.82%(white light), 12.22%(blue light), 4.33%(red light), and 6.30%(control). The crude ash contents of freeze-dried safflower sprouts were as follow as: 4.75%(white light), 4.44%(blue light), 4.00%(red light), and 3.65% (control). Crude protein contents of hot air-dried safflower sprouts were as follows: 16.52%(white light) 15.40%(blue light), 14.55%(red light), and 15.46%(control). The crude ash contents of freeze-dried safflower sprouts were as follows: 25.19%(white light), 15.72%(blue light), 25.53%(red light), and 20.13%(control). Chlorophyll contents of hot air-dried and freeze-dried safflower sprouts were higher than those of only freeze-dried sprouts. b-values of freeze-dried sprouts were lower than those of sprouts dried by other dried methods. The contents of minerals Ca, Mg, Na, P and K in all the sprout samples remains unchanged regardless of the drying methods.
This study was conducted to examine the antagonism of useful microbes against soybean sprout rotting pathogens and their effect on the growth of soybean sprouts. The antagonism against soybean sprout rotting pathogens and the effect on the growth of soybean sprouts were examined by using P. areofacience 14H-3, P. fluorescens R1-12 and B. cereus Yell, bacteria were shown to inhibit mycellial growth of Rhizotonia solani strongly. The results of this study are summarized as follows. P. areofacience 14H-3 and B. cereus Yell were highly antagonistic against Rizoctonia solani, while they were especially highly antagonistic against bacterial diseases. The effect of inhibiting the proliferation of soybean sprout rotting pathogens was also examined by adding the culture solution for antagonistic bacteria to the PDA. Both P. areofacience 14H-3 and P. fluorescens Rl-12 showed the inhibition rate of 78.8%, while B. cereus Yell did 52.9%. The fresh weight and length of soybean sprouts were measured after raising them with added antagonistic microbes and culture medium. Soybean sprouts treated with B. cereus Yell showed increased higher, compared with those not treated with it. Soybean sprouts were also raised in the culture solution with antagonistic bacteria to examine the growth of soybean sprouts. Soybean sprouts treated with the culture solution of 200 times showed better growth than those not treated with it. Analyze proximate composition in soybean sprout showed that moisture, ash, total sugar did not appear difference, but in case of crude protein B. cereus Yell(8.9%) increased about 2 times than control(3.6%), but occasion of crude fat and crude fiber were P. areofacience 14H-3, P. fluorescens Rl-12 increased about each 2 times than control. In occasion of vitamin, bacterial antagonist(9.4∼10.8mg%) was more higher than control(9.9mg%).
1. Objects The experiments of catalytic aharcoaling were carried out for the fallowing purposes. (1) To determine the economically desirable amount of catalytic materials to be used when a catalytic charcoaling is practiced. (2) To observe the rate of carbonization of non-treated charcoal wood when the catalytic charcoaling is proceeded in the same charcoal pit. 2. Meterials (1) Small sample chips made of oak (Q. accutissima Carr.), measured by 0.5cm in width and thickness, respectively, and 1cm in length, were used as charcoal wood in each experiment. (2) Ammonium chloride was used as a catalytic material and electric kiln as a charcoaling apparatus. 3. Experiment (1) The sample chips were put into a electric oven for three hours at the temperature $60^{\circ}{\sim}70^{\circ}C$ in order to reduce some water contents. (2) Oven dried sample chips were then soaked for an hour in solution of ammonium chloride. Three kinds of solution were prepared, that is, 2.5%, 5%, and 10%, solution in which the amount of ammonium chloride used was weighed at the rate of 0.5%, 1.0%, and 2.0% to the total weight of the sample chips, resppectivelly. (3) Soaked sample chips were put in the air for 12 hours to reduce some water contents, and then were put into electric oven for 2 hours at the temperature $105^{\circ}{\sim}110^{\circ}C$. (4) Dried sample chips were kept in a desiccator with control sample chips which were treated excarly the same process as the treated sample chips except only not using the ammonium chloride in the process of soking. (5) Sample chips kept in the desiccator were used at random in each charcoaling experiment. (6) Charcoaling in the electric kiln were carried out by using small crucibles with complete cover to reduce the amount of ash. At each charcoaling experiment four crucibles filled with sample ships, weighed about 20gr, were put into electric kiln. The charcoaling was continued for an hour at the temperature $400^{\circ}{\sim}450^{\circ}C$. (7) In order to investigate the influence given by the gases produced during the catalytic charcoaling to the rate of carbonization of non-treated sample chips, the following experiment was done. (a) A crueible was divided into two parts by inserting a fine iron net at the middle of the crucible, and then non-treated sample chips, weighed about 10gr, were put in the upper part of the crucible and treated sample chips, weighed also about 10gr, were put in the under part. (b) The crucibles filled with two kinds of sample chips were put into a electric kiln for an hour at the temperature $400^{\circ}{\sim}450^{\circ}C$. 4. Results. Results for two replications (with four crucibles in one replication) for each experiment designed are as follows : (1) The rats of carbonization of the non treated sample chips, and that of the treated sample chips with ammonium chloride at the rate of 1.5%, 1.0%, and 2.0% to the total weight of the sample chips used were averaged at 19.85%, 22.63%, 24.14%, and 26.60%, respectively. (2) The rats of carbonization of the non-treated sample chips were averaged at (a) 20.04% (0.5% treatment), (b) 20.28% (1.0% treatment), and (c) 20.61% (2.0% treatment) when the treated sample chips were carbonized in the same crucible.
Salt occlusion in Zeolite is a unique phenomenon that takes place only when the salt size is similar to the window size of host zeolite. $KCIO_3$-occluded Zeolite, as an environment-friendly oxidant, has a high potential for effective removal of various organic pollutants. This study was carried to investigate the characteristics and the removal kinetics of fungicide chlorothalonil by zeolite-$KCIO_3$ complex. About 10% of $KCIO_3$ was occluded in zeolite pores synthesized by salt-thermal method from fly ash, although the occlusion amount was relatively less compared to that of nitrate salts. By occlusion with $KCIO_3$, no remarkable changes were found in X-ray diffraction patterns of cancrinite, whereas some decrease of overall peak intensities was found with those of sodalite. Different releasing kinetics of $CIO_3^-$ ion were observed in distilled water and soil solution from zeolite-$KCIO_3$ complex. Two reactions, hydration and diffusion, seem to be related with the release of $KCIO_3$. Therefore, the release isotherm of $CIO_3^-$ ion well fitted to the power function model which indicate the release was made by hydration and diffusion. The removal of chlorothalonil by zeolite and $KCIO_3$ reached at reaction equilibrium within 6 hours by 18% and 47% respectively. However, the chlorothalonil removal by the zeolite-$KCIO_3$ complex increased slowly and steadily up to 92% in 96 hours. These findings suggested that zeolite-$KCIO_3$ complex could be applied for effective removal of organic contaminants in the soil and aqueous environment.
Journal of Korean Society of Environmental Engineers
/
v.35
no.5
/
pp.340-349
/
2013
The present paper investigates the availability of seawater as the absorbents to capture carbon dioxide ($CO_2$) emitted from the coal fired power plant (CFPP). For the purpose of the study, readily obtainable alkali materials in CFPP such as coal fly ash (FA), NaOH and $Ca(OH)_2$ are added to seawater to prepare the absorbents and their $CO_2$ capture performances are discussed. FA can be effectively used the additives to increase $CO_2$ capture capacity of seawater to a some extent. This is ascribed that some alkali components in FA are leached into seawater and they contribute to $CO_2$ capture in the solution. However, their leaching amount and rate are restricted by the various ions in seawater. The performance of NaOH added seawater is even lower than that of NaOH added water because $OH^-$ is substantially consumed on $Ma(OH)_2$ production prior to carbonation. $CO_2$ absorption capacity of $Ca(OH)_2$ added seawater is slightly larger than that of $Ca(OH)_2$ added water. This is because that $Ca^{2+}$ which originally present in raw seawater can participate in carbonation reaction.
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