JP5246996B2 - プラスチック分解油の処理方法 - Google Patents
プラスチック分解油の処理方法 Download PDFInfo
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- JP5246996B2 JP5246996B2 JP2005268612A JP2005268612A JP5246996B2 JP 5246996 B2 JP5246996 B2 JP 5246996B2 JP 2005268612 A JP2005268612 A JP 2005268612A JP 2005268612 A JP2005268612 A JP 2005268612A JP 5246996 B2 JP5246996 B2 JP 5246996B2
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- 238000003672 processing method Methods 0.000 title 1
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- 239000003208 petroleum Substances 0.000 claims description 27
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 24
- 229910052751 metal Inorganic materials 0.000 claims description 22
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- 238000004821 distillation Methods 0.000 claims description 16
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 15
- 239000011575 calcium Substances 0.000 claims description 13
- 239000002994 raw material Substances 0.000 claims description 13
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 12
- 229910052791 calcium Inorganic materials 0.000 claims description 12
- 229910052757 nitrogen Inorganic materials 0.000 claims description 12
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 10
- 239000000460 chlorine Substances 0.000 claims description 10
- 229910052801 chlorine Inorganic materials 0.000 claims description 10
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 9
- 239000011593 sulfur Substances 0.000 claims description 9
- 229910052717 sulfur Inorganic materials 0.000 claims description 9
- 239000010936 titanium Substances 0.000 claims description 9
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 8
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 8
- 229910052710 silicon Inorganic materials 0.000 claims description 8
- 239000010703 silicon Substances 0.000 claims description 8
- 229910052719 titanium Inorganic materials 0.000 claims description 8
- 239000002699 waste material Substances 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 7
- 229910052759 nickel Inorganic materials 0.000 claims description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 5
- 239000010949 copper Substances 0.000 claims description 5
- 150000001993 dienes Chemical class 0.000 claims description 5
- 239000011777 magnesium Substances 0.000 claims description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 4
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 4
- 229910052782 aluminium Inorganic materials 0.000 claims description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 4
- 229910052802 copper Inorganic materials 0.000 claims description 4
- 229910052749 magnesium Inorganic materials 0.000 claims description 4
- 238000005979 thermal decomposition reaction Methods 0.000 claims description 4
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims description 4
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims description 3
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims description 3
- 229910052794 bromium Inorganic materials 0.000 claims description 3
- 229910052720 vanadium Inorganic materials 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 2
- YPFNIPKMNMDDDB-UHFFFAOYSA-K 2-[2-[bis(carboxylatomethyl)amino]ethyl-(2-hydroxyethyl)amino]acetate;iron(3+) Chemical compound [Fe+3].OCCN(CC([O-])=O)CCN(CC([O-])=O)CC([O-])=O YPFNIPKMNMDDDB-UHFFFAOYSA-K 0.000 claims 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims 1
- 239000010931 gold Substances 0.000 claims 1
- 229910052737 gold Inorganic materials 0.000 claims 1
- 239000003350 kerosene Substances 0.000 description 17
- 239000003054 catalyst Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 10
- 239000007789 gas Substances 0.000 description 9
- 239000003502 gasoline Substances 0.000 description 8
- 238000004939 coking Methods 0.000 description 7
- 239000012535 impurity Substances 0.000 description 7
- 238000000197 pyrolysis Methods 0.000 description 7
- 239000000295 fuel oil Substances 0.000 description 6
- 238000005504 petroleum refining Methods 0.000 description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 125000003118 aryl group Chemical group 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000010779 crude oil Substances 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 229910052750 molybdenum Inorganic materials 0.000 description 3
- 239000011733 molybdenum Substances 0.000 description 3
- -1 polyethylene Polymers 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000004523 catalytic cracking Methods 0.000 description 2
- 238000004517 catalytic hydrocracking Methods 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 229920006122 polyamide resin Polymers 0.000 description 2
- 239000004800 polyvinyl chloride Substances 0.000 description 2
- 239000005033 polyvinylidene chloride Substances 0.000 description 2
- 229920000459 Nitrile rubber Polymers 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005443 coulometric titration Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000002795 fluorescence method Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000003348 petrochemical agent Substances 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
プラスチック分解油は、廃プラスチックの熱分解によって得られたものであり、カルシウム(Ca)の含有量が金属換算で50質量ppm以下にものが好ましく、特には10質量ppm以下、さらには2質量ppm以下が好ましい。また、チタン(Ti)及びシリコン(Si)の含有量が金属換算でそれぞれ50質量ppm以下、特には10質量ppm以下、さらには2質量ppm以下であることが好ましい。このようなプラスチック分解油は、金属含有量の少ないプラスチック分解油を選別することで得ることができる。また、廃プラスチック熱分解の原料となる廃プラスチックを選別することで金属含有量を下げることができる。
90%留出温度が100〜600℃、特には300℃を超える、さらには400℃を超えることが好ましい。
初留点は300℃以下、特には100℃以下が好ましい。
50%留出温度が100〜500℃、特には150〜350℃が好ましい。
石油留分の蒸留性状について、90%留出温度は、300〜600℃、特には400〜600℃が好ましく、プラスチック分解油の90%留出温度との差が、200℃以下、特には100℃以下であることが好ましい。石油留分の芳香族分は、10〜50%、特には20〜40%が好ましい。石油留分の90%留出温度がこの範囲であれば、石油留分中に多くの芳香族分を有し、溶解性が高いため、コーキングを抑制しながら処理できるため、好ましい。
プラスチック分解油と石油留分を混合した混合原料油は、カルシウムの含有量が金属換算で2質量ppm以下、好ましくは1質量ppm以下である。チタン及びシリコンの含有量が金属換算でそれぞれ2質量ppm以下、好ましくは1質量ppm以下であることが望ましい。
プラスチック分解油と石油留分を混合した混合原料油を処理する石油精製工程は、水素化精製、水素化分解および接触分解の少なくとも一つの工程を含むものであり、特に、水素化精製の工程が好ましい。これにより、石油留分の硫黄分、窒素分、金属分などが低減されるとともに、プラスチック分解油の窒素分、塩素分、金属分などが低減される。硫黄分が0.5〜5%、特には1%以上の石油留分をプラスチック分解油と混合して、水素化精製により硫黄分が0.2%以下、特には0.1%以下とするような精製工程が好ましい。
なお、本実施例では密度はJIS K 2249に、硫黄分はJIS K 2541(紫外蛍光法)に、窒素分はJIS K 2609(化学発光法)に、塩素分は電量滴定法、臭素価はJIS K 2605に、ジエン価はUOP 326−65に、蒸留性状はJIS K 2254、芳香族分はFIA、JPI法、金属分はICP発光分析法によって測定した。検出下限は、1質量ppmである。
Claims (3)
- 廃プラスチックの熱分解によって生成するプラスチック分解油と石油留分を混合し、水素化精製工程において処理するプラスチック分解油の処理方法であって、前記プラスチック分解油は、硫黄分が20000ppm以下、窒素分が2000ppm以下、塩素分が1〜1000ppm、臭素価が10〜300gBr 2 /100g、ジエン価が1〜5g/100gで、カルシウム、チタン、シリコン、マグネシウム、鉄、アルミニウム、銅、ニッケル及びバナジウムの含有量がそれぞれ金属換算で50質量ppm以下であり、前記石油留分は、硫黄分が0.05〜10%、窒素分が10〜5000ppm、塩素分1ppm未満、カルシウム、チタン、シリコン、マグネシウム、鉄、アルミニウム、銅、ニッケル、バナジウムの含有量がそれぞれ金属換算で500ppm以下であり、該プラスチック分解油と石油留分をプラスチック分解油の混合割合が処理対象全体に対して50容量%以下混合し、当該混合原料油は、カルシウム、チタンおよびシリコンの含有量がそれぞれ金属換算で2質量ppm以下であることを特徴とするプラスチック分解油の処理方法。
- 前記石油留分の90%留出温度と、前記プラスチック分解油の90%留出温度
との差が200℃以下である請求項1に記載のプラスチック分解油の処理方法。 - 前記石油留分の90%留出温度が、300℃を超え、600℃以下である請求
項1又は2に記載のプラスチック分解油の処理方法。
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JP2007077324A JP2007077324A (ja) | 2007-03-29 |
JP5246996B2 true JP5246996B2 (ja) | 2013-07-24 |
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US20090299110A1 (en) | 2008-05-30 | 2009-12-03 | Moinuddin Sarker | Method for Converting Waste Plastic to Lower-Molecular Weight Hydrocarbons, Particularly Hydrocarbon Fuel Materials, and the Hydrocarbon Material Produced Thereby |
WO2013070801A1 (en) * | 2011-11-10 | 2013-05-16 | Natural State Research, Inc. | Methods and systems for converting plastic to fuel |
FI128635B (en) * | 2018-12-28 | 2020-09-15 | Neste Oyj | Co-treatment procedure |
KR20230010199A (ko) | 2020-04-07 | 2023-01-18 | 토탈에너지스 원테크 벨지움 에스.에이. | 직접 접촉 분해를 통한 폐플라스틱 기반 오일의 고가 화학물질로의 승급 |
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US4778589A (en) * | 1986-08-28 | 1988-10-18 | Chevron Research Company | Decalcification of hydrocarbonaceous feedstocks using citric acid and salts thereof |
JPH10310778A (ja) * | 1997-05-12 | 1998-11-24 | Mitsubishi Oil Co Ltd | 廃プラスチック油化生成油の精製方法及び精製留分 |
JP4236548B2 (ja) * | 2003-09-29 | 2009-03-11 | 株式会社ジャパンエナジー | ナフサ留分の製造方法 |
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