• 제목/요약/키워드: Catalytic pyrolysis

검색결과 81건 처리시간 0.03초

Kinetic Analysis for the Catalytic Pyrolysis of Polyethylene Terephthalate Over Cost Effective Natural Catalysts

  • Pyo, Sumin;Hakimian, Hanie;Kim, Young-Min;Yoo, Kyung-Seun;Park, Young-Kwon
    • 공업화학
    • /
    • 제32권6호
    • /
    • pp.706-710
    • /
    • 2021
  • In the current research, thermal and catalytic thermogravimetric (TG) analysis of polyethylene terephthalate (PET) over natural zeolite (NZ), olivine, bentonite, HZSM-5, and HAl-MCM-41 were investigated using a TG analyzer and model-free kinetic analysis. Catalytic TG analysis of PET was carried out at multi-heating rates, 10, 20, 30, and 40 ℃/min, under nitrogen atmosphere. Apparent activation energy (Ea) values for the thermal and catalytic pyrolysis of PET were calculated using Flynn-Wall-Ozawa method. Although natural catalysts, NZ, olivine, and bentonite, could not lead the higher PET decomposition efficiency than synthetic zeolites, HZSM-5 and HAl-MCM-41, maximum decomposition temperatures on the differential TG (DTG) curves for the catalytic pyrolysis of PET, 436 ℃ over olivine, 435 ℃ over bentonite, and 434 ℃ over NZ, at 10 ℃/min, were definitely lower than non-catalytic pyrolysis. Calculated Ea values for the catalytic pyrolysis of PET over natural catalysts, 177 kJ/mol over olivine, 168 kJ/mol over bentonite, and 171 kJ/mol over NZ, were also not lower than those over synthetic zeolites, however, those were also much lower than the thermal decomposition, suggesting their feasibility as the proper and cost-effective catalysts on the pyrolysis of PET.

Catalytic Pyrolysis of Cellulose over SAPO-11 Using Py-GC/MS

  • Lee, In-Gu;Jun, Bo Ram;Kang, Hyeon Koo;Park, Sung Hoon;Jung, Sang-Chul;Jeon, Jong-Ki;Ko, Chang Hyun;Park, Young-Kwon
    • Bulletin of the Korean Chemical Society
    • /
    • 제34권8호
    • /
    • pp.2399-2402
    • /
    • 2013
  • The catalytic pyrolysis of cellulose was carried out over SAPO-11 for the first time. Pyrolyzer-gas chromatography/mass spectroscopy was used for the in-situ analysis of the pyrolysis products. The acid sites of SAPO-11 converted most levoglucosan produced from the non-catalytic pyrolysis of cellulose to furans. In particular, the selectivity toward light furans, such as furfural, furan and 2-methyl furan, was high. When the catalyst/cellulose ratio was increased from 1/1 to 3/1 and 5/1, the increase in the quantity of acid sites led to the promotion of deoxygenation and the resultant increase of the contents of light furan compounds. Because furans can be used as basic feedstock materials, the augmentation of the economical value of bio-oil through the catalytic upgrading over SAPO-11 is considerable.

혼합폐플라스틱 열분해 왁스오일의 고급화 연구 (A Study of Upgrading of Pyrolysis Wax Oil Obtained from Pyrolysis of Mixed Plastic Waste)

  • 이경환;남기윤;송광섭;김극태;최정길
    • 한국신재생에너지학회:학술대회논문집
    • /
    • 한국신재생에너지학회 2009년도 추계학술대회 논문집
    • /
    • pp.321-324
    • /
    • 2009
  • Upgrading of pyrolysis wax oil has been conducted in a continuous fixed bed reactor at $450^{\circ}C$, 1hour, LHSV 3.5/h. The catalytic degradation using HZSM-5 catalyst are compared with the thermal degradation and also was studied with a function of experimental variables. The raw pyrolysis wax oil shows relatively high boiling point distribution ranging from around $300^{\circ}C$ to $550^{\circ}C$, which has considerably higher boiling point distribution than that of commercial diesel. The product characteristic from thermal degradation shows a similar trend with that of raw pyrolysis wax oil. This means the thermal degradation of pyrolysis wax oil at high degradation temperature is not sufficiently occurred. On the other hand, the catalytic degradation using HZSM-5 catalyst relative to the thermal degradation shows the high conversion of pyrolysis wax oil to light hydrocarbons. This liquid product shows high gasoline range fraction as around 90% fraction and considerably high aromatic fraction in liquid product. Also, in the catalytic degradation the experimental variable such as catalyst amount and reaction temperature was studied.

  • PDF

굴참나무 촉매열분해에 바이오매스 반탄화가 미치는 영향 (The Effect of Biomass Torrefaction on the Catalytic Pyrolysis of Korean Cork Oak)

  • 이지영;이형원;김영민;박영권
    • 공업화학
    • /
    • 제29권3호
    • /
    • pp.350-355
    • /
    • 2018
  • 본 연구에서는 굴참나무의 열분해 및 촉매 열분해에 바이오매스 반탄화가 미치는 영향에 대한 연구를 수행하였다. 굴참나무와 반탄화된 굴참나무의 열분해 및 촉매 열분해 거동은 열중량분석 결과와 회분식반응기를 이용한 급속열분해 반응에서 얻어진 바이오오일의 생성물분포를 비교하여 평가하였다. 굴참나무와 반탄화된 굴참나무의 열중량 곡선 및 미중열중량곡선은 굴참나무 내 헤미셀룰로오스의 제거량은 반탄화 온도 및 시간을 증가시킴에 따라 증가됨을 나타내었다. 굴참나무의 반탄화과정에서 헤미셀룰로오스의 제거로 굴참나무 내 셀룰로오스와 리그닌의 함량이 증가되기 때문에 열분해 과정에서 오일의 수율은 감소하고 고형 촤 수율은 증가하였다. 반탄화 굴참나무의 열분해 오일 중 레보글루코산과 페놀류의 선택도는 굴참나무 열분해 오일에 비해 높았다. 바이오오일 중 방향족 화합물의 함량은 HZSM-5 ($SiO_2/Al_2O_3=30$) 상에서 굴참나무 및 반탄화된 굴참나무의 촉매열분해를 적용함으로써 증가되었다. 굴참나무에 비해, 반탄화 굴참나무는 HZSM-5를 이용한 촉매 열분해를 통한 방향족화합물 형성에 더 높은 효율을 보였고 더 높은 반탄화 온도($280^{\circ}C$) 및 반응온도($600^{\circ}C$)를 적용함으로써 극대화되었다.

Catalytic Upgrading of Geodae-Uksae 1 over Mesoporous MCM-48 Catalysts

  • Jeon, Ki-Joon;Jin, Sung Ho;Park, Sung Hoon;Jeon, Jong-Ki;Jung, Sang-Chul;Ryu, Changkook;Park, Young-Kwon
    • Bulletin of the Korean Chemical Society
    • /
    • 제35권7호
    • /
    • pp.1951-1955
    • /
    • 2014
  • Catalytic pyrolysis of Geodae-Uksae 1, a kind of miscanthus found in Korea, was carried out over mesoporous MCM-48 catalysts. For rapid product analysis and catalyst evaluation, pyrolysis-gas chromatography/mass spectrometry was used. X-ray diffraction, nitrogen sorption, pyridine adsorbed Fourier transform infrared, and NH3 temperature programmed desorption were utilized to analyze the properties of the catalysts. Compared to non-catalytic reaction, catalytic upgrading over mesoporous Al-MCM-48 catalysts produced a higher-quality bio-oil with a high stability and low oxygen content. Al-MCM-48 exhibited higher deoxygenation ability than Si-MCM-48 due to its higher acidity.

SAPO-11을 이용한 억새와 Random Polypropylene의 촉매 열분해 (Catalytic Pyrolysis of Miscanthus and Random Polypropylene over SAPO-11)

  • 강현구;유미진;박성훈;전종기;김상채;박영권
    • 폴리머
    • /
    • 제37권3호
    • /
    • pp.379-386
    • /
    • 2013
  • SAPO-11을 억새와 random polypropylene(random PP)의 촉매 열분해에 최초로 적용하였다. 열중량 분석 결과 SAPO-11은 억새의 탈수 반응을 촉진시키고, char의 생성을 억제하는 것으로 나타났다. Random PP의 열분해 결과, random PP의 분해온도와 활성화에너지는 촉매를 사용함에 따라 크게 감소하였다. 억새의 무촉매 열분해 반응에 의해 생성되는 oxygenate 생성물들 중에서 levoglucosan이 주 생성물이었다. SAPO-11 촉매 열분해 결과, 상당 부분의 levoglucosan이 furans, phenolics, aromatics 등의 부가가치가 큰 화합물로 전환하였다. 반면, random PP는 가솔린, 디젤 범위의 탄화수소를 생성하였다.

활엽수재(闊葉樹材)의 촉매적(触媒的) 열분해(熱分解) 생성물(生成物)에 관한 연구(硏究) (Studies on the Catalytic Pyrolysis Products of Hardwood)

  • 민두식;이종관
    • 한국산림과학회지
    • /
    • 제65권1호
    • /
    • pp.12-23
    • /
    • 1984
  • 재료(材料)는 충북대학교 구내에서 생육하는 물오리나무, 상수리나무, 아카시아나무, 은수원시시나무재(材)의 톱밥을 이용하고 촉매제(觸媒劑)는 무기염류(無機鹽類)인 연안(憐安), 유안(硫安), 염안(鹽安) 및 요소(尿素)를 농도별(濃度別)로 처리(處理)하여 건류(乾溜)함으로써 얻어지는 유출생성물(溜出生成物)과 건류탄(乾溜炭)의 생성량(生成量)과 건류탄(乾溜炭)의 품질(品質)에 미치는 발열량(發熱量)을 조사(調査)한 시험(試驗)이다. 1) Holocellulose와 pentosan 함유량이 가장 많은 수종은 은수원사시나무재(材)였으며 촉매제(觸媒劑)로 연안처리(憐安處理)를 한 것이 은수원자시나무 재(材)에서 건류(乾溜) 유출액생성량(溜出液生成量)도 많았다. 2) 촉매제(觸媒劑)의 농도(濃度)가 높을수록 건류(乾溜) 액상생성물량(液狀生成物量)은 감소하였으며 무처리재(無處理材)의 것이 가장 많은 유출액생성량(溜出液生成量)을 보여주고 있다. 3) 건류탄(乾溜炭) 생성량(生成量)은 촉매제(觸媒劑)의 농도(濃度)가 높을수록 증가(增加)하였으며 Lignin 함유량(含有量)이 많은 수종(樹種)일수록 건류탄생성량(乾溜炭生成量)도 많았다. 4) 촉매제(觸媒劑)의 종류(種類)에 의한 건류탄(乾溜炭)의 발열량(發熱量)에는 큰 차이(差異)가 없었으나 촉매제(觸媒劑)의 농도(農度)가 높은 것일수록 발열량(發熱量)은 감소되었다. 그러나 촉매제(觸媒劑)의 종류별(種類別)로 생성(生成)된 건류탄(乾類炭)의 발열량간(發熱量間)에는 유의차(有意差)가 인정(認定)되지 않았다.

  • PDF

LDPE 반회분식 촉매열분해에서 조업조건이 반응 특성에 미치는 영향 (Effects of Reaction Conditions on the Performance of Catalytic Pyrolysis of LDPE in a Semi-Batch Reactor)

  • 나정걸;임철현;최휘경;정수현
    • 한국신재생에너지학회:학술대회논문집
    • /
    • 한국신재생에너지학회 2006년도 추계학술대회
    • /
    • pp.79-82
    • /
    • 2006
  • Fueled by ballooning oil prices, waste plastics are now regarded as being cheap and abundant renewable sources, removing their stigma of dirty wastes Catalytic pryolysis of plastics in liquid phase allows recovery of light fuel oil as well as green treatment of polymerics wastes, and therefore significant efforts have been devoted to this research field. In this study, catalytic Pyrolysis of LDPE was carl ied out in semi-batch reactor which equipped a unit of separation and recirculation. The effect of react ion conditions were examined by analyzing liquid oil yield and carbon number distribution of products

  • PDF

Emulsification of the Mixture of Catalytic Pyrolysis Oil Obtained under Methane and Nitrogen Environment in Diesel Using Span 80 and Atlox 4916 as Surfactants

  • Farooq, Abid;Park, Young-Kwon
    • 공업화학
    • /
    • 제32권3호
    • /
    • pp.357-360
    • /
    • 2021
  • Emulsions were prepared using a mixture of bio-oil obtained from the pyrolysis of sawdust in an N2 environment and Quercus mongolica in a CH4 environment for both non-catalytic and catalytic cases. Both prepared emulsions were examined by measuring the physical stability and Fourier transform infrared spectroscopy. The emulsion with HLB 5.8 (Span 80 and Atlox 4916) for the ratio of bio-oil (B-oil and C-oil): surfactant: diesel = 10% : 3% : 87% showed stability for 15 days. Combining oils produced in N2 and CH4 environments could be a potential solution for generating high-quality emulsions with a high heating value.