• Current Research on Agriculture and Life Sciences
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• v.8
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• pp.29-34
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• 1990

This study was conducted to examine the influence of heat treatment on the $NH_4{^+}$ adsorption by zeolite and to determine the $NH_4{^+}$ loss from $NH_4-$ zeolite during the incubation. The dominant clay minerals of zeolite were clinoptiloiite and mordenite. $NH_4{^+}$ adsorption by zeolite was equilibrated at a 4hrs-shaking. The content of exchangeable $K^+$ of zeolite was increased with increase in the temperature of heat treatment but the amount of $NH_4{^+}$ adsorbed by zeolite was decreased. The amount of $NH_4{^+}$ in the soil treated with ammonium sulfate was decreased during incubation under the submerged condition but the amount of $NH_4{^+}$ adsorbed by zeolite was not decreased in the same course of incubation. It was estimated that $NH_4{^+}$ adsorbed by zeolite was resistant to $NH_4{^+}$-N loss by various reactions.

• KOREAN JOURNAL OF PACKAGING SCIENCE & TECHNOLOGY
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• v.3 no.2
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• pp.25-31
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• 1996

Various treaments such heating, acid tenting, acid healing, alkaline treating, acid+alkaline renting were attempted to investigate their effects on molar ratio, chemical composition, DTA and specific surface area(SSA) of natural zeolite poder. Molar ratio, Si to AI. of natural zeolite was 4.78, which represented high silica type. Composition of natural zeolite showed that $SiO_2$ was 66.34% $Al_2O_3$ was 13.89%, $Fe_2O_2$ was 1.55% X-ray diffraction showed that main component of natural zeolite was mordenite and clinoptliolite. Differential Thermal Analysis and Thermogravimetry curve of natural zeolite was showed to peak of endothermic peak at $80^{\circ}C$ and it means to the peak of dehydrate reaction, but recristalization was not formed below at $1,000^{\circ}C$. Weight loss during calcination was 16% at $1,000^{\circ}C$. Thermal treatments on SSA of natural zolite powder decreased from $75.2m^2/g\;to\;2.1m^2/g$. In contrast chemical treatments on SSA showed to increase to $300.2m^2/g$(1 N HCl treating), $54.9m^2/g$(1 N NaOH) and $90.9m^2/g$(HCl+NaOH)tudy, it could be proposed to employ acid tret method as packaging materisls for MA packaging.

• Korean Journal of Environmental Agriculture
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• v.10 no.1
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• pp.11-19
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• 1991

This study was carried out to develop the low-priced adsorbent by synthesizing the zeolite of high CEC with the natural zeolite and examining the ability of this zeolite to adsorb heavy metals. The dominant clay minerals were clinoptilolite and mordenite in natural zeolite, while phillipsite in the synthesized zeolite. Adsorption reaction of Cu and Zn on clays were reached to equilibrium after 1 hr. The amount of adsorption was increased as the concentrations of heavy metals or the initial pH of suspension was increased. The synthesized zeolite adsorbed heavy metals about twice as much as the natural zeolite. The adsorption of heavy metals on the synthesized zeolite was less affected by the initial pH of suspension than that on natural zeolite. At cumulative adsorption, the synthesized zeolite adsorbed much more heavy metals at early three treatments than the natural zeolite did. The amount of desorption by chloride salts was increased as the concentration of chloride salts was increased. The ability of salt to desorb was in the order of NaCl>$CaC1_2$>$AlC1_3$. It is estimated that the ability of the synthesized zeolite to remove heavy metals was better than that of the natural zeolite.

• Applied Chemistry for Engineering
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• v.23 no.3
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• pp.320-325
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• 2012

The catalytic cracking of waste lubricant oil was carried out on silica-alumina (SA), hydrogen-type mordenite (HM), and dealuminated mordenite (DM) with the silica/alumina ratio of 10.5, 10, and 12.5, respectively. Activity in the catalytic cracking was found to be in the order of SA > DM > HM. Carbon number distribution of the oil obtained over SA was similar to that of gasoline while that of the oil obtained over DM was similar to that of diesel. Carbon number distribution of the oil obtained over HM was similar to that between gasoline and diesel. Acid amounts of three kinds of catalysts were found to be in the order of $SA\;{\approx}\;HM$ > DM. Unlike HM and DM with pores of an uniform diameter below 10 A, SA had a pore size distribution within the range of 10 to 50 A. These results indicate that the acid amount and pore size of the catalysts may be related to the carbon number distribution of the cracked oil. The decrement of surface area by the accumulation of carbon and impurities on the surface of the catalyst was found to be in the order of SA > DM > HM.

• Journal of Korean Society of Environmental Engineers
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• v.39 no.2
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• pp.51-58
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• 2017

We investigated the efficiency of natural zeolite with different cation exchange capacity (CEC) as capping material for the remediation of marine sediments contaminated with heavy metals. Three different zeolite with high CEC (HCzeo, 163.74 cmolc/kg), medium CEC (MCzeo, 127.20 cmolc/kg), and low CEC (LCzeo, 70.62 cmolc/kg) were used. The surface area of the zeolite was in decreasing order: HCzeo ($59.43m^2/g$) > MCzeo ($52.10m^2/g$) > LCzeo ($10.12m^2/g$). The results of mineralogical composition obtained from X-ray diffraction (XRD) show that LCzeo was mainly composed of quartz and albite. In the XRD result of MCzeo and HCzeo, the peaks of clinoptilolite, heulandite, and mordenite were also observed along with that of quartz and albite. Sorption equilibrium onto the HCzeo, MCzeo, and LCzeo was reached in 6 h at initial concentration of 10 mg/L and 100 mg/L. Higher adsorption of Cd and Zn onto the zeolite with higher CEC were achieved but adsorption of Cu and Ni were not dependent on the CEC of zeolite. It can be concluded that the zeolite with high cation exchange ability is recommended for the contaminated sediments with Cd and Zn but the inexpensive zeolite with low CEC for Cu and Ni.

• Membrane Journal
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• v.29 no.5
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• pp.263-275
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• 2019

In the present study, thickness of MOR zeolite membranes was controlled by changing seed size, seeding amount, and aging time of hydrothermal solution, and then effect of membrane thickness on pervaporative ethanol dehydration for 90 wt.% ethanol-water mixture was investigated. First, nanosize MOR zeolite seeds with a diameter of 20 to 30 nm was successfully prepared by planetary milling a laboratory synthesized MOR zeolites and the coating amount was controlled by seed concentration and infiltration volume of coating solution during vacuum-assisted seeding. As seeding amount decreased, membrane thickness was reduced up to around $4{\mu}m$. The MOR zeolite membrane having a thickness of $4{\mu}m$ showed a water/ethanol separation factor of 760 and water flux of $1.0kg/m^2h$. The excellent water flux was due to the reduced membrane thickness which was derived from the nanosize seed. Therefore, it could be concluded that membrane thickness control by using nanosize seed can be a crucial factor to improve pervaporative water flux of MOR zeolite membrane.

• Journal of the Korean Chemical Society
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• v.17 no.1
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• pp.47-52
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• 1973

Korean bentonite was treated with aqueous NaOH solution under the reaction conditions such as concentration of NaOH, 0.5-6N; ratio of $Na_{2}O$ to $SiO_2$, 1-4; reaction time, 2-30 days; reaction temperature, $70^{\circ}C-90^{\circ}C$. The products were examined by X-ray diffraction patterns. When it was treated with 2N NaOH at $70^{\circ}C$, zeolite species $P_1$ was formed with good yield. In higher concentration and at higher temperature than above, zeolite species $P_1$ was converted to hyeroxysodalite. Together with these crystals, some faujasite type zeolite, sodium A zeolite, mordenite type zeolite etc. was formed depending upon reaction conditions.

• YAKHAK HOEJI
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• v.34 no.5
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• pp.302-310
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• 1990

A study has been made of the Korean bentonite aqueous suspension contrast with American bentonite by means of XRD IR swelling, gel formation and rheogram at various conditions such as concentration, temperature and pH. The Korean bentonite was identified as montmorillonite clay containig a small proprotion of crystoballite and mordenite, and its swelling power were acceptable for requirements of Korean pharmacopeia regulations though its values were not satisfied. Korean bentonite swelled to 10 times and American one did to 15 times compared to its bulkiness of powder. The rheogram of Korean bentonite suspension reveals bulged pseudoplatic flow with yield value at higher concentration and pseudoplastic flow without yield value at lower concentration. The higher the concentration, the greater were the apparent viscosity and hysteresis loop. Korean bentonite suspension showed insignificant temperature dependence on both apparent viscosity and hysteresis loop and it was more temperature dependent on viscosity but less on hysteresis loop than those of American sample. The pH dependence was so high on viscosity that apparent minimum value was near pH 7 and maximum value at pH 3 or 7. The hysteresis loop appeared minimum over the pH range 5-7 and maximum near pH 3 or 11. The Korean bentonite was inferior to the American bentonite in swelling volume, gel formation, thioxotropy, however, it would be possible to improve the quality of Korean bentonite by developing the method of purification for bentonite clay.

• Economic and Environmental Geology
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• v.16 no.3
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• pp.149-161
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• 1983

Fuller's earth deposits from Miocene sedimentary sequences in Gyeong Sang-do contain up to 95% Ca-montmorillonite accompanied by cristobalite, clinoptilolite, mordenite, quartz, feldspar and X-ray amorphous material. Differential thermal analysis, infrared and electron microscopic data are given for the montmorillonite component. The ease with which the exchangeable calcium of the montmorillonite could be replaced by sodium (to give a product with properties similar to that of a bentonite) was monitored by the Atterberg liquid limit test. Some samples tested as possible binders for foundry moulding sands gave results that compared favourably with material currently being used for this application. Many of the samples also met the OCMA specifications for clays used in drilling muds.

• Applied Biological Chemistry
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• v.25 no.2
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• pp.99-104
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• 1982

Natural zeolite rock was pulverized and dispersed in water. Clay fraction was collected by sedimentation method. The dominant clay mineral was Clinoptiolite with some Mordenite and Smectite. $P^{32}$ adsorption on Na-zeolite was determined in different ionic strengths using $P^{32}$ isotope by sludge method. The lower the pH of suspension, the longer the contact time, and the more the amount of zeolite, the more inorganic P was adsorbed by Na-zeolite, whereas the more P adsorption per unit gram of zeolite was observed at a 100mg addition than a 200mg in same volume of P-NaCl solution (20ml), indicating that the whole positively charged surface of Na-zeolite was not occupied by inorganic P. Furthermore, the more P adsorption on Na-zeolite was observed in higher ionic strength than in the lower. The maximum P adsorption on Na-zeolite was about 1me/g, and the zero point charge (ZPC) is assumed to be below pH 3.7.