• Title/Summary/Keyword: carbonization yield

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Preparation and Characterization of ACF Using Lyocell Adopting Surface Modification Process (리오셀 표면개질공정을 도입한 ACF 제조 및 특성)

  • Jo, Young Hyuk;Jin, Young Min;Lee, Soon Hong
    • Journal of the Korean Society of Safety
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    • v.31 no.1
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    • pp.66-73
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    • 2016
  • Lyocell fibers were used as a precursor in order to improve yield and strength of cellulose-based precursor while manufacturing activated carbon fiber(ACF). Lyocell fibers as a precursor for the preparation of ACF were surface-modified by reaction with 3-aminopropyltriethoxysilane(APTES) and pre-treated with KOH and H3PO4. Using aforementioned precursor, ACFs were prepared by a series of stabilization, carbonization and activation process at high temperatures. On each process, FT-IR, TGA, UTM and SEM were used to observe fibers' physical properties including structure and porous surfaces. FT-IR results proved that surface modification was achieved during stabilization, carbonization and activation process. TGA results during carbonization process found that surface modified fibers with APTES 0.02 mol(A2) showed higher thermostability, and extended pre-treatment increased yield. Especially, yield was found to have an increase of 10~20 wt% with surface modification during activation process. UTM results showed that tensile strength has the same order of concentration of APTES after surface modification, however, was found to show lower tensile strength than lyocell fibers after stabilization process. SEM results revealed that more homogeneous porosity control could be proceed after modifying the surface for the effective removal of hazardous substances.

Properties of Clay-Woodceramics from 3 layers-clay-woodparticleboard (점토목재파티클보드로 제조된 Clay-Woodceramics의 성질)

  • Lee, Hwa Hyoung;Kim, Gwan Eui
    • Journal of the Korean Wood Science and Technology
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    • v.31 no.5
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    • pp.80-87
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    • 2003
  • This research was carried out to examine physical and mechanical properties of clay-woodceramics which were carbonized for 3 hours in a special furnace from 3 layers-clay-woodparticleboard made from pallet waste wood, phenol formaldehyde resin(hereafter PF, Non volatile content 52%, resin content 30%) and clay(10%, 20% and 30%). Carbonization temperature was 400℃, 600℃ and 800℃. The results are summarized as follows: 1. The higher the carbonization temperature, the higher the dimensional shrinkage and the lower the carbonization yield ratio. But the higher the clay addition, the lower the dimensional shrinkage and the higher carbonization yield ratio. 2. The higher the carbonization temperature, the higher the water absorption and the density. The higher the clay content, the higher the density. 3. The higher the carbonization temperature, the higher the bending Modulus of Rupture and bending Modulus of Elasticity.

An Energy Characteristics of Carbonization Residue produced from Sewage Sludge Cake (하수슬러지 케익으로부터 생산한 탄화물의 에너지 특성)

  • Rhee, Seung-Whee
    • Korean Chemical Engineering Research
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    • v.47 no.2
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    • pp.230-236
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    • 2009
  • Sewage sludge cake(SSC) is seriously concerned because ocean dumping, which is the cheapest treatment method now, will be banned in 2012. On the basis of this reason, recycling of SSC is emphasized to convert the treatment method. One of the method to recycling SSC could be carbonization process which also can be reduced greenhouse gas effectively. And carbonization residue of SSC produced by carbonization process can become a renewable energy source. However, carbonization process has not been evaluated by considering basic operating data such as heating value, yield and fuel ratio. In this study, the basic characteristics of SSC such as proximate analysis, elementary analysis and heating value are analyzed. In carbonization process, the effect of carbonization temperature and time on the residue of SSC are estimated. And the analysis is carried out to obtain basic properties of the residue of SSC. From the result of chemical composition of SSC residue, there is 27% of phosphate in SSC. Phosphate will take a role of reductant to convert from hazardous substance to non-hazardous material. As increased carbonization temperature and time, heating value and yield are decreased but fuel ratio(fixed carbon/volatile combustible) of the residue is increased. In the carbonization process, the optimum temperature and time in carbonization test for SSC can be decided by $250^{\circ}C$ and 15 min, respectively. However, the carbonization residue of SSC can not be deserved to use one of renewable energy sources because the heating value at the optimum condition is relatively low. Hence, it is desirable that SSC can be mixed with other organic waste to carbonize.

Study on the Adsorbent using Waste - Food Waste - (폐기물을 이용한 흡착제에 관한 연구 - 음식물 폐기물 -)

  • 박흥재;정성욱;이봉헌
    • Journal of Environmental Science International
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    • v.11 no.10
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    • pp.1097-1101
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    • 2002
  • Activated carbon is amorphous and its intraparticle pores are well developed. Thus it has high adsorption capabilities and catalytic effect, and is utilized in many areas of industries such as food processing. In recent years, the demand of activated carbon has been increased to solve the environmental problems-waste treatment and removal of poisonous gas. Therefore, in this study an activated carbon was made using the waste and then the industrial characteristics of the produced activated carbon were investigated. The result showed that the carbonization yield was decreased when carbonization temperature was increased from 400 to $600^{\circ}C$ and that the optimal carbonization temperature was $500^{\circ}C$. The optimal concentration of NaOH for removing ash in the raw sample was 1~2N. The iodine adsorption of activated carbon using waste sample at $500^{\circ}C$ carbonization was 1204.28mg/g. The activation result of carbonization sample showed that the optimal activation condition was the carbonization at $500^{\circ}C$ and the activation at $800^{\circ}C$. So the production of activated carbon was thought to be possible, reused as resource, and decreased the environmental pollution.

Efficient Carbonization of ABS Rubber via Iodine Doping

  • Park, Chiyoung;Kim, Chae Bin
    • Elastomers and Composites
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    • v.57 no.1
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    • pp.9-12
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    • 2022
  • Herein, a facile approach for the development of effective and low-cost carbon precursors from acrylonitrile-butadiene-styrene (ABS) rubber is reported. ABS rubber with a negligible char yield can be converted into an excellent carbon precursor with approximately 54% char yield under a nitrogen atmosphere at 800℃ by simple iodine doping and subsequent heating at 110℃ under an inert atmosphere. The enhanced char yield is attributed to the improved intermolecular interactions between the ABS chains caused by the formation of covalent bonds between the butadiene segments, along with the newly developed charge-charge interactions and other indiscriminate radical-radical couplings. The charges and radicals involved in these interactions are also generated by iodine doping. We believe that this study will be useful for the development of low-cost carbon precursors.

The Properties of carbonized and activated RDF (탄화 및 활성화된 RDF의 특성 연구)

  • Choi, Yeong-Seok
    • 한국신재생에너지학회:학술대회논문집
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    • 2006.11a
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    • pp.87-90
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    • 2006
  • The experimental study has been done for two kinds of pelletized RDFs to Investigate the carbonization effect to the chlorine concentrations, the heating value and the yield of Produced char in variable conditions of the carbonizing temperature and reaction time. One(RDF-1) is made of 100% wasted plastics and the other(RDF-2) is made of 60% wasted paper with 40% wasted plastics. The screw type carbonizer heated Indirectly by oil burner was used for the experiment and RDF feeding rate was 3kg/hr. The carbonizing temperature was 300, 350 400 and $45^{\circ}C$ and the reaction tine was 5, 10 and 15 minutes respectively. As the increase of carbonizing reaction time and temperature, the chlorine reduction rate was increased and oppositely the yield of char was decreased At the temperature of $400^{\circ}C$ and reaction time of 10 minutes the chlorine reduction rate was 60% and the char yield rate was 80% for the RDF-1 and those of RDF-2 were 80% and 75%, respectively. Additional activation experiment to the char produced from RDF-2 was done in the activation reactor by hot steam supply. As the increase of activation time the iodine number was increased. At the activation time of 20 minutes the iodine number was 552mg/g and the yield of activated carbon was 16%.

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Charcoal Properties and Temperature Change of a Kiln's Inner and Outer Walls in Carbonization Process Using an Improved Kiln (개량형탄화로를 이용한 제탄과정 중 탄화로 내·외벽 온도변화 및 목탄 특성)

  • Kwon, Gu-Joong;Kwon, Sung-Min;Jang, Jae-Hyuk;Hwang, Won-Joung;Kim, Nam-Hun
    • Journal of the Korean Wood Science and Technology
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    • v.39 no.3
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    • pp.230-237
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    • 2011
  • The study was performed to investigate the characteristics of charcoal and temperature change of a kiln's inner and outer walls in carbonization process using improved kiln. In this kiln system, carbonization process was completed in eight days. In the kiln, the ignition temperature was kept about $720^{\circ}C$. And then the temperature were increased gradually prior to be refined. Finally, the temperature in refining process was reached to maximum point, $1,000^{\circ}C$. In the chimney, the temperature was increased gradually from $90^{\circ}C$ at ignition to $750^{\circ}C$ at refining. The temperature change of the kiln wall resembles a temperature change progress curve during a carbonization process. The highest temperature of the kiln wall that appeared by a carbonization process was around $500^{\circ}C$. As a result of having measured an inner wall and the outer wall of the kiln using an infrared thermography camera, it was judged with there being considerable latent heat on kiln wall and ceiling. Fixed carbon contented of charcoal was 85.9~89.9%. Refining degree of charcoal, hardness, calorific value and pH were l, 12, 7,047~7,456 kcal/kg, 9.0~9.9, respectively. The yield of wood charcoal was 13.8%, and compared to conventional kiln's yield increased 1.5%.

Preparation and Characterization of PAN-based Web of Carbon Nanofibers by Electrostatic Spinning

  • Kim, Chan;Yang, Kap-Seung
    • Carbon letters
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    • v.3 no.4
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    • pp.210-218
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    • 2002
  • Electrostatic spinnings were performed with the solutions of PAN/DMF to be nanofiber webs. The diameter of the fibers ranged from 200 nm to 1000 nm depending on the PAN concentration and on the applied DC voltage. The nanofibers were oxidatively stabilized and subsequently carbonized up to $1000^{\circ}C$ with carbonization yield of 40%. The bulk electric conductivity of the carbonized web increased form $6.8{\times}10^{-3}S/cm$ to 1.96 S/cm while the carbonizaton temperature increased from $700^{\circ}C$ to $1000^{\circ}C$.

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Densification of 4D Carbon Fiber Performs with Mesophase Pitch as Matrix-Precursor

  • Joo, Hyeok-Jong;Lee, Jae-Won
    • Carbon letters
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    • v.6 no.3
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    • pp.173-180
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    • 2005
  • In this study, AR (aromatic resin) pitch was employed as the matrix-precursor for carbon/carbon composite because it exhibits much higher coke yield than coal tar pitch. As a result, a fabrication process of carbon/carbon composites can be shortened. It has been known that the pitches may cause swolling problem during the carbonization process. In order to restrain the swelling occurrence, a small quantity of carbon black was added to the AR pitch. Due to addition of carbon black the swelling was decreased largely and the perform can be infiltrated with the AR pitch. The densification efficiency of the performs was compared with various matrix-precursors. The coke yield of matrixprecursors, the morphology and the degree of graphitization of carbon matrix were analyzed.

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A comparison study of extraction methods for bio-liquid via hydrothermal carbonization of food waste

  • Bang, YeJin;Choi, Minseon;Bae, Sunyoung
    • Analytical Science and Technology
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    • v.31 no.3
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    • pp.112-121
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    • 2018
  • The hydrothermal carbonization method has received great attention because of the conversion process from biomass. The reaction produces various products in hydrochar, bio-liquid, and gas. Even though its yield cannot be ignored in amount, it is difficult to find research papers on bio-liquid generated from the hydrothermal carbonization reaction of biomass. In particular, the heterogeneity of feedstock composition may make the characterization of bio-liquid different and difficult. In this study, bio-liquid from the hydrothermal carbonization reaction of food wastes at $230^{\circ}C$ for 4 h was investigated. Among various products, fatty acid methyl esters were analyzed using two different extraction methods: liquid-liquid extraction and column chromatography. Different elutions with various solvents enabled us to categorize the various components. The eluents and fractions obtained from two different extraction methods were analyzed by gas chromatography with a mass spectrometer (GC/MS). The composition of the bio-liquid in each fraction was characterized, and seven fatty acid methyl esters were identified using the library installed in GC/MS device.