• Title/Summary/Keyword: 열 분해

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Carbon Dioxide-based Plastic Pyrolysis for Hydrogen Production Process: Sustainable Recycling of Waste Fishing Nets (이산화탄소 기반 플라스틱 열분해 수소 생산 공정: 지속가능한 폐어망 재활용)

  • Yurim Kim;Seulgi Lee;Sungyup Jung;Jaewon Lee;Hyungtae Cho
    • Korean Chemical Engineering Research
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    • v.62 no.1
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    • pp.36-43
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    • 2024
  • Fishing net waste (FNW) constitutes over half of all marine plastic waste and is a major contributor to the degradation of marine ecosystems. While current treatment options for FNW include incineration, landfilling, and mechanical recycling, these methods often result in low-value products and pollutant emissions. Importantly, FNWs, comprised of plastic polymers, can be converted into valuable resources like syngas and pyrolysis oil through pyrolysis. Thus, this study presents a process for generating high-purity hydrogen (H2) by catalytically pyrolyzing FNW in a CO2 environment. The proposed process comprises of three stages: First, the pretreated FNW undergoes Ni/SiO2 catalytic pyrolysis under CO2 conditions to produce syngas and pyrolysis oil. Second, the produced pyrolysis oil is incinerated and repurposed as an energy source for the pyrolysis reaction. Lastly, the syngas is transformed into high-purity H2 via the Water-Gas-Shift (WGS) reaction and Pressure Swing Adsorption (PSA). This study compares the results of the proposed process with those of traditional pyrolysis conducted under N2 conditions. Simulation results show that pyrolyzing 500 kg/h of FNW produced 2.933 kmol/h of high-purity H2 under N2 conditions and 3.605 kmol/h of high-purity H2 under CO2 conditions. Furthermore, pyrolysis under CO2 conditions improved CO production, increasing H2 output. Additionally, the CO2 emissions were reduced by 89.8% compared to N2 conditions due to the capture and utilization of CO2 released during the process. Therefore, the proposed process under CO2 conditions can efficiently recycle FNW and generate eco-friendly hydrogen product.

Study on the decomposition of 1,1,2-trichloroethane in a pyrolysis reactor and a numerical study for scale-up design (열분해 반응기에서 1,1,2-trichloroethane의 분해특성과 Scale-up 설계를 위한 수치해석적 연구)

  • 이채복;라승혁;강경태;김상용
    • Proceedings of the Korea Air Pollution Research Association Conference
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    • 2002.11a
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    • pp.417-418
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    • 2002
  • 열분해는 독성이 강한 염화탄화수소의 처리뿐만 아니라 염화물을 효과적으로 제거하여 이들로부터 유용한 탄화수소를 얻을 수 있는 반응이다 Biomass에 열분해를 적용하여 가스상, 액상, 고상형태의 유동한 부산물로 전환시키고 있으며 현재 액상생성물은 외국에서 큰 주목을 받고 있는 부산물이다. 1,1,2-trichloroethane(TCE)는 독성이 강한 휘발성 유기화합물(VOC)이며 발암물질이다. (중략)

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A Study on the Pyrolysis Processing for sludge disposal in sewage treatment plant (하수처리장내 슬러지 처리를 위한 열분해공정에 관한 연구)

  • Ha, Sang-An;Kim, Hyeoog-Seok;Sung, Nak-Chang
    • Journal of the Korea Organic Resources Recycling Association
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    • v.10 no.4
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    • pp.65-74
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    • 2002
  • This Study was investigated operating condition of pyrolysis processing for sludge disposal in sewage treatment plant. Important parameters studied include running time of pyrolysis, run time of dry and pyrolysis processing, water content of sewage sludge, solids amount of sewage sludge(TS%), condition of pyrolysis temperature. Most degradation reaction of sewage sludge are first order, it assumed first order and elucidated the kinetics. This was the basis of characteristics analysis of sludge degradation mechanism. Also, with the increasing of temperature, how the yield of oil and char product change was observed, and the distribution of gas product components was observed. Main components of gas and carbon product are a little difference with pyrolysis temperature, but it consist of $CH_4$, $C_2H_4$, $C_3H_8$, $C_4H_{10}$, toluene, $C_6H_6$, $SO_2$, CO etc. The gas of $C_1-C_4$ yield increased along with degradation temperature of $670^{\circ}C$ and oil yield decreased of $C_6H_6$ and $C_6H_5OH$ with temperature of $600^{\circ}C$. Particularly, low value added char yield 134kg/t at $670^{\circ}C$, but increased to 194kg/t at pyrolysis temperature of $600^{\circ}C$. In the result of elementary analysis on it, it is mainly composed of carbon. From this fact, in pyrolysis of sludge, it comfirmed that carbonization reaction occur at high temperature well.

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Study on the Pyrolysis Kinetics of Deasphalted Oil Using Thermogravimetric Analysis (열중량 분석법을 이용한 Deasphalted Oil의 열분해 특성 분석)

  • Shin, Sang Cheol;Lee, Jung Moo;Lee, Ki Bong;Jeon, Sang Goo;Na, Jeong Geol;Nho, Nam Sun
    • Korean Chemical Engineering Research
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    • v.50 no.3
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    • pp.391-397
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    • 2012
  • The depletion of conventional oil reserves and the increasing energy need in developing countries such as China and India result in exceeding oil demand over supply. As a solution of the problem, the efficient utilization of heavy oil has been receiving more and more interest. In order to utilize heavy oil, upgrading processes are required. Among the upgrading processes, thermal decomposition is thought to be relatively simple and economical. In this study, to understand basic characteristics of thermal decomposition of heavy oil, we conducted pyrolysis experiments of deasphalted oil (DAO) produced by a solvent deasphalting process. DAO is a mixture of many components and consists mainly of materials of carbon number 20~40. For the comparison with results of DAO pyrolysis, additional pyrolysis experiments with single materials of carbon number 30 ($C_{30}H_{62}$, $C_{30}H_{58}O_4S$, $C_{30}H_{63}O_3P$) were conducted. Pyrolysis experiments were carried out non-isothermally with variation of heating rate (10, 50, $100^{\circ}C$/min) in a thermogravimetric analyzer. Average pyrolysis activation energy determined by using Arrhenius method, Ingraham and Marrier method, and Coats and Redfern method was 72~99 kJ/mol. In the activation energy calculated by Ozawa-Flynn-Wall method, DAO had wider variation than other single materials.

Distribution Characteristics of Pyrolysis Products of Polyethylene (폴리에틸렌 열분해 생성물의 분포 특성)

  • Lee, Dong-Hwan;Choi, Hong-Jun;Kim, Dae-Su;Lee, Bong-Hee
    • Polymer(Korea)
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    • v.32 no.2
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    • pp.157-162
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    • 2008
  • To investigate the characteristics of pyrolysis for LDPE, LLDPE and HDPE, the low temperature pyrolysis was carried out in the range of 425 to $500^{\circ}C$ for 35 to 65 min. The liquid products formed during pyrolysis were classified into gasoline, kerosene, light oil and wax according to the distillation temperatures based on the petroleum product quality standard of Korea Petroleum Quality Inspection Institute. TGA experiments for three PE samples showed that the onset temperature of pyrolysis increased with increasing heating rate, and the onset temperature of pyrolysis at a fixed heating rate was in the order of LDPE$475^{\circ}C$. Yields of gasoline and kerosene were highest at $450^{\circ}C$, 65 min and decreased slightly at above $475^{\circ}C$.

Thermal Denitration of High Concentration Nitrate Salts Waste Water (열분해에 의한 고농도 질산염 폐액의 탈질)

  • ;;;;;C. Latge
    • Proceedings of the Korean Radioactive Waste Society Conference
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    • 2003.11a
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    • pp.665-670
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    • 2003
  • This study investigated the thermodynamic and the thermal decomposition properties of high concentration nitrate salts waste water for the lagoon sludge treatment. The thermodynamic property was carried out by COACH and GEMINI II based on the composition of nitrate Salts waste water. The thermal decomposition property was carried out by TG-DTA and XRD. Ammonium nitrate and sodium nitrate were decomposed at $250^{\circ}C$$730^{\circ}C$$450^{\circ}C$$Na_2O$ into stable $Na_2O$.$Al_2O_3$. The flow sheet for nitrate salts waste water treatment was proposed based on the these properties data. These will be used by the basic data of the process simulation.

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Study on the Liquefaction Characteristics of ABS Resin in a Low-Temperature Pyrolysis (ABS 수지의 저온 열분해에 의한 액화특성 연구)

  • Choi, Hong Jun;Jeong, Sang Mun;Lee, Bong-Hee
    • Korean Chemical Engineering Research
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    • v.49 no.4
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    • pp.417-422
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    • 2011
  • The low temperature pyrolysis of ABS resin has been carried out in a batch reactor under the atmospheric pressure. The effect of the reaction temperature on the yield of pyrolytic oils has been determined in the present study. The oil products formed during pyrolysis were classified into gas, gasoline, kerosene, gas oil and heavy oil according to the petroleum product quality standard of Ministry of Knowledge Economy. The conversion reaches 80% after 60 min at $500^{\circ}C$ in the pyrolysis of ABS resin. The amount of the final product was ranked as gas heavy oil > gasoline > gas oil > kerosen based on the yield. The yields of heavy oil and gas oil increase with an increase in the reaction time and temperature.

Adsorption Characteristics of Heavy Metal and VOCs of Pyrolysis Char from Organic Waste Sludge (유기성 폐슬러지의 열분해 차르에 대한 중금속 및 VOCs 흡착특성)

  • Park, Sang-Sook;Kang, Hwa-Young
    • Journal of Korean Society of Environmental Engineers
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    • v.27 no.2
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    • pp.130-137
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    • 2005
  • This research programme include investigation of the adsorption behavior of heavy metals and VOCs by Pyrolysis char for using landfill cover material. The volatile potions in the sludge gasified during the pyrolysis period and gave birth to porosity throughout the matrix. The result of the ad/desorption experiment of nitrogen to find out the formation of some pore by the gasification of the volatile matter, we can certify that the pyrolysis char($14.56\;m^2/g$) has increased twice more than the organic wasted sludge($6.68\;m^2/g$) in specific surface area. The pyrolysis char has the adsorption characteristic of medium type of Type II and V in BDDT classification, and showed a little micro pore. In the adsorption experiment of ethylbenzene and toluene, as a result of applying the Freundlich adsorption isotherms, the pyrolysis char was higher in the adsorptivity of ethylbenzene and toluene than the granite and the organic wasted sludge. The results of the heavy metal adsorption test for the char indicated that it had some ability of adsorption. It is suggest that pyrolysis char has some advantages for utilizing as landfill covers because the pyrolysis char can adsorb/absorb hazardous substances from the landfill sites and inhibit the ground water and soil contamination.

Preparation of Bio-oil from Ginkgo Leaves through Fast Pyrolysis and its Properties (은행잎 바이오매스로부터 급속 열분해를 통한 바이오-오일 생산 및 특성 연구)

  • In-Jun Hwang;Jae-Rak Jeon;Jinsoo Kim;Seung-Soo Kim
    • Clean Technology
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    • v.29 no.3
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    • pp.200-216
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    • 2023
  • Ginkgo leaves are considered waste biomass and can cause problems due to the strong insecticidal actions of ginkgolide A, B, C, and J and bilobalide. However, Ginkgo leaf biomass has high organic matter content that can be converted into fuels and chemicals if suitable technologies can be developed. In this study, the effect of pyrolysis temperature, minimum fluidized velocity, and Ginkgo leaf size on product yields and product properties were systematically analyzed. Fast pyrolysis was conducted in a bubbling fluidized bed reactor at 400 to 550℃ using silica sand as a bed material. The yield of pyrolysis liquids ranged from 33.66 to 40.01 wt%. The CO2 and CO contents were relatively high compared to light hydrocarbon gases because of decarboxylation and decarbonylation during pyrolysis. The CO content increased with the pyrolysis temperature while the CO2 content decreased. When the experiment was conducted at 450℃ with a 3.0×Umf fluidized velocity and a 0.43 to 0.71 mm particle size, the yield was 40.01 wt% and there was a heating value of 30.17 MJ/kg, respectively. The production of various phenol compounds and benzene derivatives in the bio-oil, which contains the high value products, was identified using GC-MS. This study demonstrated that fast pyrolysis is very robust and can be used for converting Ginkgo leaves into fuels and thus has the potential of becoming a method for waste recycling.

A Study on Pyrolysis of Silane and Disilane at Low Pressure (저압에서의 사알렌과 디사일렌의 열분해 반응에 관한 연구)

  • 한재현;문상흡
    • Journal of the Korean Vacuum Society
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    • v.4 no.4
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    • pp.350-357
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    • 1995
  • SiH4와 Si2H6를 1-3 Torr 정도의 저압에서 열분해시켰을 때, 반응물의 농도 변화를 살펴보고 이로부터 열분해의 반응 기구를 예측하였다. 분석기로는 질량 분석기를 이용하였으며, 분해 온도 범위는 SiH4의 경우는 $350~475^{\circ}C$, Si2H6의 경우는 275-375$^{\circ}C$이었다. SiH4의 분해 양상은 1차 비가역 반응에 잘 들어 맞았으며, 그 속도 상수는 문헌에 보고되어 있는 상압에서의 속도보다 작았다. Si2H6는 낮은 온도 범위에서도 잘 분해되었으며, 중간 생성물로 많은 양의 SiH4를 만들었다. 그리고, SiH4는 고분자화되는 반응을 거치지 않고 고체실리콘을 생성하지만, Si2H6는 중간 생성물로 만들어진 SiH4와 SiH2에 의하여, 고분자화 반응을 거쳐서 고체실리콘을 만들 수 있음을 알았다.

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