JP2023552232A - 液化廃棄物ポリマーを処理するための方法 - Google Patents
液化廃棄物ポリマーを処理するための方法 Download PDFInfo
- Publication number
- JP2023552232A JP2023552232A JP2023539374A JP2023539374A JP2023552232A JP 2023552232 A JP2023552232 A JP 2023552232A JP 2023539374 A JP2023539374 A JP 2023539374A JP 2023539374 A JP2023539374 A JP 2023539374A JP 2023552232 A JP2023552232 A JP 2023552232A
- Authority
- JP
- Japan
- Prior art keywords
- naphtha
- distillate
- lwp
- hydrotreating
- reaction conditions
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 46
- 239000002699 waste material Substances 0.000 title claims abstract description 27
- 229920000642 polymer Polymers 0.000 title claims abstract description 16
- 150000001993 dienes Chemical class 0.000 claims abstract description 32
- 238000004821 distillation Methods 0.000 claims abstract description 30
- 239000010779 crude oil Substances 0.000 claims abstract description 21
- 238000006243 chemical reaction Methods 0.000 claims description 21
- 239000003054 catalyst Substances 0.000 claims description 18
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 14
- 239000001257 hydrogen Substances 0.000 claims description 14
- 229910052739 hydrogen Inorganic materials 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 14
- 239000003921 oil Substances 0.000 claims description 13
- 239000004033 plastic Substances 0.000 claims description 13
- 229920003023 plastic Polymers 0.000 claims description 13
- 238000009835 boiling Methods 0.000 claims description 10
- 238000000197 pyrolysis Methods 0.000 claims description 7
- 229910003294 NiMo Inorganic materials 0.000 claims description 6
- 239000004215 Carbon black (E152) Substances 0.000 claims description 4
- 229930195733 hydrocarbon Natural products 0.000 claims description 4
- 150000002430 hydrocarbons Chemical class 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- 239000000341 volatile oil Substances 0.000 claims description 3
- 150000001336 alkenes Chemical class 0.000 abstract description 4
- 238000005504 petroleum refining Methods 0.000 abstract description 3
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 239000012535 impurity Substances 0.000 description 8
- 239000012071 phase Substances 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 229910052593 corundum Inorganic materials 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229910001845 yogo sapphire Inorganic materials 0.000 description 3
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 2
- 229910052794 bromium Inorganic materials 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 238000004939 coking Methods 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 125000005842 heteroatom Chemical group 0.000 description 2
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000006298 dechlorination reaction Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 229910052752 metalloid Inorganic materials 0.000 description 1
- 150000002738 metalloids Chemical class 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000010817 post-consumer waste Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
- C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
- C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/002—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/32—Selective hydrogenation of the diolefin or acetylene compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/88—Molybdenum
- B01J23/882—Molybdenum and cobalt
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/88—Molybdenum
- B01J23/883—Molybdenum and nickel
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
Description
a)ジオレフィンおよびナフサを含むLWPストリームを提供する工程、
b)ジオレフィンおよびナフサを含む蒸留物ならびに蒸留塔底物を得るために、LWPストリームを水蒸気ストリッパーに付す工程、
c)ジオレフィン枯渇蒸留物を生成するために、水素および1または複数の水素化処理触媒の存在下、蒸留物を水素化処理反応条件に付す工程、ならびに
d)ジオレフィン枯渇蒸留物を、
大気圧下で180℃より低い温度で沸騰する少なくとも1つのナフサ留分、および任意には大気圧下で180℃~360℃の間で沸騰する中間留分を含む1または複数の留分と、
塔底留分と
に分離する工程。
a)ジオレフィンおよびナフサを含むLWPストリームを提供する工程、
b)ジオレフィンおよびナフサを含む蒸留物ならびに蒸留塔底物を得るために、LWPストリームを水蒸気ストリッパーに付す工程、
c)ジオレフィン枯渇蒸留物を生成するために、水素および1または複数の水素化処理触媒の存在下、蒸留物を水素化処理反応条件に付す工程、
d)ジオレフィン枯渇蒸留物を、
大気圧下で180℃より低い温度で沸騰する少なくとも1つのナフサ留分、および任意には大気圧下で180℃~360℃の間で沸騰する中間留分を含む1または複数の留分と、
塔底留分と
に分離する工程、ならびに
e)水素および1または複数の水素処理触媒の存在下、工程d)のナフサ留分を水素処理反応条件に付す工程。
a)ジオレフィンおよびナフサを含むLWPストリームを提供する工程、
b)ジオレフィンおよびナフサを含む蒸留物ならびに蒸留塔底物を得るために、LWPストリームを水蒸気ストリッパーに付す工程、
c)ジオレフィン枯渇蒸留物を生成するために、水素および1または複数の水素化処理触媒の存在下、蒸留物を水素化処理反応条件に付す工程、
d)ジオレフィン枯渇蒸留物を、
大気圧下で180℃より低い温度で沸騰する少なくとも1つのナフサ留分、および任意には大気圧下で180℃~360℃の間で沸騰する中間留分を含む1または複数の留分と、
塔底留分と
に分離する工程、ならびに
e)水素および1または複数の水素処理触媒の存在下、ナフサ留分を水素処理反応条件に付す工程。
カラム内でジオレフィンによって引き起こされるファウリングが減少される。
水蒸気ストリッピングは、LWP中に存在する金属の大部分を蒸留塔底物に蓄積させ、これゆえ、ナフサ中の低い金属含有量を実現している。これにより、ジオレフィン除去触媒が保護され、その寿命が延長される。
工程b)の蒸留塔底物、ならびに、工程d)の塔底留分および任意の中間留分は、主にジオレフィンを含まないため、粗油と混合され得、および石油精製におけるフィードとして使用され得る。
Claims (19)
- 液化廃棄物ポリマー(LWP)を処理するための方法であって、以下の工程:
a)ジオレフィンおよびナフサを含むLWPストリームを提供する工程、
b)ジオレフィンおよびナフサを含む蒸留物ならびに蒸留塔底物を得るために、LWPストリームを水蒸気ストリッパーに付す工程、
c)ジオレフィン枯渇蒸留物を生成するために、水素および1または複数の水素化処理触媒の存在下、蒸留物を水素化処理反応条件に付す工程、ならびに
d)ジオレフィン枯渇蒸留物を、
大気圧下で180℃より低い温度で沸騰する少なくとも1つのナフサ留分、
任意には、大気圧下で180℃~360℃の間で沸騰する中間留分
を含む1または複数の留分と、
塔底留分と
に分離する工程
を含む方法。 - e)水素化ナフサを製造するために、水素および1または複数の水素処理触媒の存在下、前記工程d)の前記ナフサ留分を水素処理反応条件に付す工程
を含む請求項1記載の方法。 - 前記工程b)の前記水素化処理反応条件が、120~210℃の温度および1~50bargの圧力を含む請求項1または2記載の方法。
- 前記水素化処理反応条件が、1~5h-1、好ましくは4~4.5h-1であるLHSVを含む請求項3記載の方法。
- 前記1または複数の水素化処理触媒が、CoMoおよびNiMoから選択される請求項1~4のいずれか1項に記載の方法。
- 前記工程e)の前記水素処理反応条件が、280~350℃の温度および20~100barg、好ましくは20~50bargの圧力を含む請求項2~5のいずれか1項に記載の方法。
- 前記水素処理反応条件が、1~5h-1のLHSV、および、100~900Nm3/m3の水素/炭化水素比を含む請求項6記載の方法。
- 前記1または複数の水素処理触媒が、CoMoおよびNiMoから選択される請求項2~7のいずれか1項に記載の方法。
- 前記水素化ナフサをスチームクラッカーに供給する工程を含む請求項2~8のいずれか1項に記載の方法。
- 混和物を製造するために、前記工程d)の塔底留分と粗油とを混和する工程を含む請求項1~9のいずれか1項に記載の方法。
- 前記混和物を粗油蒸留ユニットに供給する工程を含む請求項10記載の方法。
- 前記工程d)の前記1または複数の留分が、大気圧下で180℃~360℃の間で沸騰する中間留分を含む請求項1~11のいずれかに記載の方法。
- 前記中間留分を粗油蒸留ユニットに供給する工程を含む請求項12記載の方法。
- 前記LWPが、廃プラスチック熱分解油および水熱液化廃プラスチック油またはそれらの混合物から選択される請求項1~13のいずれか1項に記載の方法。
- 前記LWPが、廃プラスチック熱分解油を含む請求項1~14のいずれか1項に記載の方法。
- 請求項2~8のいずれか1項に記載の方法にしたがって製造される水素化ナフサの、スチームクラッカーフィードとしての使用。
- 粗油と工程d)の塔底留分との混合物の、精油フィードとしての使用。
- 粗油と工程d)の中間留分との混合物の、精油フィードとしての使用。
- 粗油と工程b)の蒸留塔底物との混合物の、精油フィードとしての使用。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI20206385A FI130067B (fi) | 2020-12-30 | 2020-12-30 | Menetelmä nesteytettyjen jätepolymeerien prosessoimiseksi |
FI20206385 | 2020-12-30 | ||
PCT/FI2021/050732 WO2022144491A1 (en) | 2020-12-30 | 2021-10-29 | Method for processing liquefied waste polymers |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2023552232A true JP2023552232A (ja) | 2023-12-14 |
JP7466067B2 JP7466067B2 (ja) | 2024-04-11 |
Family
ID=78536241
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2023539374A Active JP7466067B2 (ja) | 2020-12-30 | 2021-10-29 | 液化廃棄物ポリマーを処理するための方法 |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP4211203A1 (ja) |
JP (1) | JP7466067B2 (ja) |
KR (1) | KR102620209B1 (ja) |
CN (1) | CN116568779A (ja) |
CA (1) | CA3192960C (ja) |
FI (1) | FI130067B (ja) |
WO (1) | WO2022144491A1 (ja) |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4311034A1 (de) | 1993-04-03 | 1994-10-06 | Veba Oel Ag | Verfahren zur Gewinnung von Chemierohstoffen und Kraftstoffkomponenten aus Alt- oder Abfallkunststoff |
US5904838A (en) * | 1998-04-17 | 1999-05-18 | Uop Llc | Process for the simultaneous conversion of waste lubricating oil and pyrolysis oil derived from organic waste to produce a synthetic crude oil |
JP2009242555A (ja) | 2008-03-31 | 2009-10-22 | Mitsui Eng & Shipbuild Co Ltd | 廃プラスチックの処理方法及び処理装置 |
US8067656B2 (en) * | 2008-11-26 | 2011-11-29 | Chevron U.S.A. Inc. | Liquid-liquid separation process via coalescers |
US8569561B2 (en) | 2009-08-06 | 2013-10-29 | Shell Oil Company | Method for revamping an HF or sulphuric acid alkylation unit |
US8920755B2 (en) * | 2011-09-12 | 2014-12-30 | Chevron U.S.A. Inc. | Conversion of HF alkylation units for ionic liquid catalyzed alkylation processes |
US9656185B2 (en) | 2012-07-11 | 2017-05-23 | Merichem Company | Contactor and separation apparatus and process of using same |
FI126029B (en) | 2013-10-17 | 2016-05-31 | Upm Kymmene Corp | Process for the preparation of hydrocarbons |
WO2015128033A1 (en) * | 2014-02-25 | 2015-09-03 | Saudi Basic Industries Corporation | Process for converting mixed waste plastic (mwp) into valuable petrochemicals |
US9932530B2 (en) | 2014-06-17 | 2018-04-03 | Air Products And Chemicals, Inc. | Refining used motor oil through successive hydrotreating processes |
US9522859B2 (en) | 2014-12-11 | 2016-12-20 | Uop Llc | Methods for recovering ionic liquid fines from a process stream |
WO2016142809A1 (en) | 2015-03-10 | 2016-09-15 | Sabic Global Technologies, B.V. | A robust integrated process for conversion of waste plastics to final petrochemical products |
WO2016142808A1 (en) | 2015-03-10 | 2016-09-15 | Sabic Global Technologies, B.V. | An integrated process for conversion of waste plastics to final petrochemical products |
EP3095843A1 (en) * | 2015-05-21 | 2016-11-23 | Neste Oyj | Method for producing bio hydrocarbons by thermally cracking a bio-renewable feedstock containing at least 65 wt.% iso-paraffins |
US10308896B2 (en) * | 2015-08-10 | 2019-06-04 | The Procter & Gamble Company | Methods for producing alkylbenzenes, paraffins, olefins and oxo alcohols from waste plastic feedstocks |
EP3491103B1 (en) * | 2016-08-01 | 2023-08-02 | SABIC Global Technologies B.V. | A catalytic process of simultaneous pyrolysis of mixed plastics and dechlorination of the pyrolysis oil |
WO2018055555A1 (en) * | 2016-09-22 | 2018-03-29 | Sabic Global Technologies, B.V. | An integrated process configuration involving the steps of pyrolysis, hydrocracking, hydrodealkylation and steam cracking |
-
2020
- 2020-12-30 FI FI20206385A patent/FI130067B/fi active IP Right Grant
-
2021
- 2021-10-29 KR KR1020237010590A patent/KR102620209B1/ko active IP Right Grant
- 2021-10-29 WO PCT/FI2021/050732 patent/WO2022144491A1/en active Application Filing
- 2021-10-29 JP JP2023539374A patent/JP7466067B2/ja active Active
- 2021-10-29 EP EP21805558.0A patent/EP4211203A1/en active Pending
- 2021-10-29 CA CA3192960A patent/CA3192960C/en active Active
- 2021-10-29 CN CN202180083410.5A patent/CN116568779A/zh active Pending
Also Published As
Publication number | Publication date |
---|---|
FI130067B (fi) | 2023-01-31 |
US20230392084A1 (en) | 2023-12-07 |
KR20230050468A (ko) | 2023-04-14 |
CN116568779A (zh) | 2023-08-08 |
EP4211203A1 (en) | 2023-07-19 |
KR102620209B1 (ko) | 2024-01-02 |
JP7466067B2 (ja) | 2024-04-11 |
CA3192960A1 (en) | 2022-07-07 |
CA3192960C (en) | 2024-05-07 |
FI20206385A1 (en) | 2022-07-01 |
WO2022144491A1 (en) | 2022-07-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US10550342B2 (en) | Integrated process for increasing olefin production by recycling and processing heavy cracker residue | |
JP6215936B2 (ja) | 炭化水素供給原料の熱水蒸気分解による転化方法 | |
JP6415588B2 (ja) | 高沸点炭化水素供給原料をより軽沸点の炭化水素生成物に転換する方法 | |
AU2013301887B2 (en) | Process for converting hydrocarbon feeds to olefin-containing product streams by thermal steamcracking | |
JP6181181B2 (ja) | 分解炉における熱水蒸気分解によってオレフィンを製造する方法 | |
JP6184496B2 (ja) | 熱水蒸気分解によるオレフィンの製造方法 | |
CN109790475B (zh) | 用于由原油生产化学原料的系统和方法 | |
JP5425373B2 (ja) | 炭化水素油の分解方法 | |
JP7466067B2 (ja) | 液化廃棄物ポリマーを処理するための方法 | |
JP7466066B2 (ja) | 液化廃棄物ポリマーを処理するための方法 | |
US12006480B2 (en) | Method for processing liquefied waste polymers | |
WO2021055540A1 (en) | Methods for producing needle coke from aromatic recovery complex bottoms | |
JP4409977B2 (ja) | 石油精製における廃油処理方法 | |
KR20240073975A (ko) | 폐플라스틱의 처리 방법 | |
JP2005325263A (ja) | オレフィン類の製造方法 | |
WO2021101557A1 (en) | Process for treating coal derived liquids by separate processing of polar and non-polar compounds | |
KR20160080167A (ko) | 폐중질유의 정제방법 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20230911 |
|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20230911 |
|
A871 | Explanation of circumstances concerning accelerated examination |
Free format text: JAPANESE INTERMEDIATE CODE: A871 Effective date: 20230911 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20231212 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20240312 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20240326 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20240401 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 7466067 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |