JP2018524324A - メチルtert−ブチルエーテル(MTBE)及び炭化水素の製造方法 - Google Patents
メチルtert−ブチルエーテル(MTBE)及び炭化水素の製造方法 Download PDFInfo
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- JP2018524324A JP2018524324A JP2017566126A JP2017566126A JP2018524324A JP 2018524324 A JP2018524324 A JP 2018524324A JP 2017566126 A JP2017566126 A JP 2017566126A JP 2017566126 A JP2017566126 A JP 2017566126A JP 2018524324 A JP2018524324 A JP 2018524324A
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- ethylene
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- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical group CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims abstract description 63
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- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 claims abstract description 33
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- CXBDYQVECUFKRK-UHFFFAOYSA-N 1-methoxybutane Chemical compound CCCCOC CXBDYQVECUFKRK-UHFFFAOYSA-N 0.000 description 1
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- FUJCRWPEOMXPAD-UHFFFAOYSA-N lithium oxide Chemical compound [Li+].[Li+].[O-2] FUJCRWPEOMXPAD-UHFFFAOYSA-N 0.000 description 1
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- KPFOFXWYYUNJOZ-UHFFFAOYSA-L nickel(2+);tributylphosphane;dichloride Chemical compound Cl[Ni]Cl.CCCCP(CCCC)CCCC.CCCCP(CCCC)CCCC KPFOFXWYYUNJOZ-UHFFFAOYSA-L 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/04—Ethylene
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/08—Alkenes with four carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/08—Alkenes with four carbon atoms
- C07C11/09—Isobutene
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
- C07C2/08—Catalytic processes
- C07C2/14—Catalytic processes with inorganic acids; with salts or anhydrides of acids
- C07C2/20—Acids of halogen; Salts thereof ; Complexes thereof with organic compounds
- C07C2/22—Metal halides; Complexes thereof with organic compounds
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/1516—Multisteps
- C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/48—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by oxidation reactions with formation of hydroxy groups
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/02—Monohydroxylic acyclic alcohols
- C07C31/04—Methanol
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
- C07C4/04—Thermal processes
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
- C07C41/01—Preparation of ethers
- C07C41/05—Preparation of ethers by addition of compounds to unsaturated compounds
- C07C41/06—Preparation of ethers by addition of compounds to unsaturated compounds by addition of organic compounds only
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C43/00—Ethers; Compounds having groups, groups or groups
- C07C43/02—Ethers
- C07C43/03—Ethers having all ether-oxygen atoms bound to acyclic carbon atoms
- C07C43/04—Saturated ethers
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Abstract
【選択図】 図1
Description
本出願は、2015年6月22日に出願された米国仮出願第62/183,014号、及び2016年6月3日に出願された米国正規出願第15/173,042号に対する優先権の利益を主張し、特許協力条約に基づいて出願され、これらの全文が参考として本明細書に組み込まれる。
本明細書において、用語“アルキル化する”または“アルキル化”は、C3−C5オレフィンを強酸触媒の存在下でイソブタンと結合させるなど、アルキル基を1つの分子からまた他の分子に移動させることを意味する。
エチレンを、触媒(二塩化ニッケルトリ−n−ブチルホスフィン)を含む二量体化反応器に0.129kg/分の速度で供給し、二塩化エチルアルミニウムを0.098kg/分の速度でさらに導入した。ヘキサン中の触媒の溶液を使用した。二量体化反応器は、約1586kPaの圧力及び約48℃の温度で操作した。
本質的にエタンからなり、プロパンなどの不純物が約10重量%未満の供給物を、約815℃〜約870℃の温度で約100kPa〜約170kPaの圧力で分解させた。分解生成物を冷却した後、約70kPaで油焼入れを行い、続いて約38℃で水焼入れを行い、その後に、約3600kPaの圧力で圧縮を行った。圧縮ストリームを約16℃に冷却し、乾燥させた後、少なくとも約−151℃の温度に冷却しながら、部分的には段階的に凝縮して、前記圧縮ストリームから高純度の水素ストリームを分離した。その後、残留炭化水素から蒸留により脱メタン塔からの塔頂(overhead)生成物としてメタンを分離した。
エチレンストリームを約38℃の温度、約1030kPaの圧力及び約30分の滞留時間で操作されるエチレン二量体化反応器に通過させ、二塩化エチルアルミニウム及びニッケル塩−ホスフィン錯体の混合物を使用して反応を触媒した。反応をクエンチングし、残存する触媒を除去した後、二量体化生成物を約110℃の塔底温度及び480kPaで分別蒸留させ、C5及び重質炭化水素を自動車ガソリン生成物として除去し、ブチレン−リッチストリームを生成した。ブチレン−リッチストリームを周囲温度及び約414kPaの圧力で分子篩吸着剤を使用して乾燥させた。
二量体化ユニットを約1165kPaの圧力、約30分の滞留時間及び約70ppmの触媒(二塩化エチルアルミニウムとニッケル塩−ホスフィン錯体を含む)濃度で操作した。温度を約34℃から約43℃に上昇させると、エチレン転換率は、約92%から約95%に増加した。しかしながら、選択性は、約94.5%から約92%に低下した。
二量体化ユニットを約1103kPaの固定圧力、約15分の滞留時間及び約43℃の温度で操作した。触媒(二塩化エチルアルミニウムとニッケル塩−ホスフィン錯体を含む)組成を約5ppmから約30ppmに増加させると、エチレン転換率は約97.5%から約99.3%に増加した。
二量体化ユニットを約483kPaの固定圧力、約20分の滞留時間及び約10ppmの触媒(二塩化エチルアルミニウムとニッケル塩ホスフィン錯体を含む)濃度で操作した。温度を約52℃から約43℃に低下させると、ブテンの選択性は約81.5%から約87.2%に増加した。
反応器は、先ず予熱帯域に不活性充填材で充填された。使用された不活性充填材は、小さなメッシュの鋼玉石(corundum)または不活性粘土触媒担持体ボールのベッドのうちのいずれかの1つである。不活性ベッドの深さは、触媒が占める熱電対地点に依存して変化した。典型的な充填(loading)深さは不活性材料の約75cmだった。
実施例VIIIは、触媒が水素フェリエライトであり、約96gが充填されることを除いては、実施例VIIに記載された順序に従って実行された。圧力は約103kPa〜約117kPaであり、時間当たりの重量空間速度は約15であった。
Claims (11)
- メチルt−ブチルエーテルの製造方法であって:
エタンまたはプロパンを含む原料を分解してエチレンを生成し、残存する未分解原料を回収することを含む第1のステップ;
エチレンを二量体化してn−ブチレンを生成することを含む第2のステップ;
前記n−ブチレンを異性化してイソブチレンを生成することを含む第3のステップ;
メタンを酸化させてメタノールを生成することを含む任意選択の第4のステップ;
前記イソブチレンをメタノールでエーテル化させてメチルt−ブチルエーテルを生成することを含む第5のステップ;及び
前記メチルt−ブチルエーテルを収集することを含む第6のステップ、を含む、方法。 - 前記第2のステップは:
未転換エチレンを回収し;
n−ブチレンをイソブタンでアルキル化してアルキレートガソリンを生成し;及び
前記アルキレートガソリンを回収することをさらに含む、請求項1に記載の方法。 - 前記第2のステップは:
未転換エチレンを回収し;
少なくとも3つのエチレン分子などの組み合わせを二量体化して高分子量エチレンオリゴマーを生成し;及び
前記高分子量エチレンオリゴマーを回収することをさらに含む、請求項1に記載の方法。 - 前記第5のステップは:
高分子量エチレンオリゴマーをメタノールでエーテル化して高分子量−エチレン−オリゴマー系メチルエーテルを生成し;及び
前記高分子量−エチレン−オリゴマー系メチルエーテルを回収することをさらに含む、請求項3に記載の方法。 - 前記第3のステップは:
未転換n−ブチレンを回収し;
高分子量エチレンオリゴマーを異性化し;
前記異性化された高分子量エチレンオリゴマーを回収することをさらに含む、請求項3に記載の方法。 - 前記第5のステップは:
異性化された高分子量エチレンオリゴマーをメタノールでエーテル化して異性化された高分子量−エチレン−オリゴマー系メチルエーテルを生成し;及び
前記異性化された高分子量−エチレン−オリゴマー系メチルエーテルを回収することをさらに含む、請求項5に記載の方法。 - 前記第3のステップは:
未転換n−ブチレンを回収し;
イソブチレンをイソブタンでアルキル化してアルキレートガソリンを生成し;及び
アルキレートガソリンを回収することをさらに含む、請求項1に記載の方法。 - 前記任意選択の第4のステップは:
未転換メタンを回収することをさらに含む、請求項1に記載の方法。 - メチルt−ブチルエーテルの製造方法であって:
エタンまたはプロパンを含む原料を分解してエチレンを生成し;及び残存する未分解原料を回収することを含む任意選択の第1のステップ;
エチレンを二量体化してn−ブチレンを生成し;
前記未転換エチレンを回収し;
n−ブチレンをイソブタンでアルキル化してアルキレートガソリンを生成し;
前記アルキレートガソリンを回収し;
少なくとも3つのエチレン分子などの組み合わせを二量体化して高分子量エチレンオリゴマーを生成し;及び
前記高分子量エチレンオリゴマーを回収することを含む第2のステップ;
前記n−ブチレンを異性化してイソブチレンを生成し;
未転換n−ブチレンを回収し;
イソブチレンをイソブタンでアルキル化してアルキレートガソリンを生成し;
アルキレートガソリンを回収し;
高分子量エチレンオリゴマーを異性化し;及び
前記異性化された高分子量エチレンオリゴマーを回収することを含む第3のステップ;
メタンを酸化させてメタノールを生成し;及び
未転換メタンを回収することを含む任意選択の第4のステップ;
イソブチレンをメタノールを以てエーテル化してメチルt−ブチルエーテルを生成し;
高分子量エチレンオリゴマーをメタノールでエーテル化して高分子量−エチレン−オリゴマー系メチルエーテルを生成し;
前記高分子量−エチレン−オリゴマー系メチルエーテルを回収し;
異性化された高分子量エチレンオリゴマーをメタノールを以てエーテル化して異性化された高分子量−エチレン−オリゴマー系メチルエーテルを生成し;及び
前記異性化された高分子量−エチレン−オリゴマー系メチルエーテルを回収することを含む第5のステップ;及び
前記メチルt−ブチルエーテルを回収することを含む第6のステップ、を含む、方法。 - アルキレートガソリンを製造する方法であって:
エタンまたはプロパンを含む原料を分解してエチレンを生成し;
エチレンを二量体化してn−ブチレンを生成し;
前記n−ブチレンを異性化させてイソブチレンを生成し;
n−ブチレンをイソブタンでアルキル化してアルキレートガソリンを生成し;及び
アルキレートガソリンを回収することを含む、方法。 - エタンまたはプロパンを含む原料を分解してエチレンを生成させるステップは、残存する未分解原料を回収することをさらに含む、請求項10に記載の方法。
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4731490A (en) * | 1986-07-23 | 1988-03-15 | Arco Chemical Company | Process for methyl, tertiary butyl ether production |
US5260499A (en) * | 1992-01-14 | 1993-11-09 | Phillips Petroleum Company | Ethylene dimerization and catalyst therefor |
JPH0711267A (ja) * | 1993-05-28 | 1995-01-13 | Inst Fr Petrole | 炭素原子を5〜8個有するオレフィンを含む炭化水素留分のエーテル化を含む方法により得られる発動機燃料 |
WO1997032901A1 (en) * | 1996-03-08 | 1997-09-12 | Phillips Petroleum Company | Method for the production of ether and alkylate from a paraffin feedstock |
US5990370A (en) * | 1997-09-24 | 1999-11-23 | Bp Chemicals Limited | Steam cracking of ethane-rich and propane-rich streams |
JP2010007152A (ja) * | 2008-06-30 | 2010-01-14 | National Institute Of Advanced Industrial & Technology | メタノールの製造方法及びその製造装置 |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL133290C (ja) * | 1962-11-30 | 1900-01-01 | ||
US3326866A (en) | 1963-06-10 | 1967-06-20 | Mobil Oil Corp | Sulfonated resin catalyst with enhanced activity |
US4242531A (en) | 1978-08-14 | 1980-12-30 | Phillips Petroleum Company | Olefin dimerization |
US4760210A (en) * | 1981-01-27 | 1988-07-26 | Sweeney Maxwell P | Partial oxidation system |
DE3124293A1 (de) * | 1981-06-19 | 1983-01-05 | Bayer Ag, 5090 Leverkusen | Verfahren zur herstellung von reinen alkyl-tert.-alkylethern und weitgehend vom isoolefin und vom alkanol befreiten kohlenwasserstoff-raffinaten |
EP0091232B1 (en) | 1982-04-06 | 1985-07-10 | Exxon Research And Engineering Company | Butene dimerization method |
CN1057451A (zh) * | 1986-07-29 | 1992-01-01 | 美孚石油公司 | 一种醚的制备方法 |
US4992613A (en) | 1989-08-16 | 1991-02-12 | Shell Oil Company | Double-bond isomerization process using basic zeolite catalysts |
US6323384B1 (en) | 1991-06-05 | 2001-11-27 | Equistar Chemicals, Lp | Process for isomerizing linear olefins to isoolefins |
US5320993A (en) | 1992-07-17 | 1994-06-14 | Phillips Petroleum Company | Dimerization catalyst systems and processes |
US5260449A (en) * | 1992-08-12 | 1993-11-09 | E. R. Squibb & Sons, Inc. | Method for preparing 7-oxabicycloheptyl substituted bromooxazole amide prostaglandin analog intermediates useful in the preparation of anti-thrombotic and anti-vasospastic compounds |
US5659090A (en) * | 1993-10-15 | 1997-08-19 | Institut Francais Du Petrole | Steps in a process for the production of at least one alkyl tertiobutyl ether from natural gas |
FR2711136B1 (fr) * | 1993-10-15 | 1996-02-02 | Inst Francais Du Petrole | Procédé de production d'au moins un alkyl tertiobutyl éther à partir du gaz naturel. |
US20040249229A1 (en) | 2003-06-06 | 2004-12-09 | Gee Jeffery C. | Isomerization of olefins with carboxylic acid |
US7271308B2 (en) | 2004-10-19 | 2007-09-18 | Hercules Incorporated | Process for isomerization of alpha olefins to internal olefins |
US7432408B2 (en) | 2004-12-21 | 2008-10-07 | Chevron U.S.A. Inc. | Integrated alkylation process using ionic liquid catalysts |
US8395005B2 (en) * | 2010-10-13 | 2013-03-12 | Equistar Chemicals, Lp | Production of 1-butene and propylene from ethylene |
US20130066130A1 (en) | 2011-09-12 | 2013-03-14 | Chevron U.S.A. Inc. | Ionic liquid catalyzed alkylation processes & systems |
-
2016
- 2016-06-03 US US15/173,042 patent/US10364204B2/en active Active
- 2016-06-21 CA CA2990185A patent/CA2990185C/en active Active
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- 2016-06-21 KR KR1020187000557A patent/KR102336488B1/ko active IP Right Grant
- 2016-06-21 EP EP16741422.6A patent/EP3310747B1/en active Active
- 2016-06-21 JP JP2017566126A patent/JP6846364B2/ja active Active
- 2016-06-21 CN CN201680036208.6A patent/CN107771172A/zh active Pending
- 2016-06-21 WO PCT/US2016/038558 patent/WO2016209831A1/en active Application Filing
- 2016-06-21 MX MX2017017038A patent/MX2017017038A/es unknown
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- 2016-06-21 MY MYPI2017704652A patent/MY182154A/en unknown
- 2016-06-21 EA EA201890033A patent/EA034976B1/ru unknown
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4731490A (en) * | 1986-07-23 | 1988-03-15 | Arco Chemical Company | Process for methyl, tertiary butyl ether production |
US5260499A (en) * | 1992-01-14 | 1993-11-09 | Phillips Petroleum Company | Ethylene dimerization and catalyst therefor |
JPH0711267A (ja) * | 1993-05-28 | 1995-01-13 | Inst Fr Petrole | 炭素原子を5〜8個有するオレフィンを含む炭化水素留分のエーテル化を含む方法により得られる発動機燃料 |
WO1997032901A1 (en) * | 1996-03-08 | 1997-09-12 | Phillips Petroleum Company | Method for the production of ether and alkylate from a paraffin feedstock |
US5990370A (en) * | 1997-09-24 | 1999-11-23 | Bp Chemicals Limited | Steam cracking of ethane-rich and propane-rich streams |
JP2010007152A (ja) * | 2008-06-30 | 2010-01-14 | National Institute Of Advanced Industrial & Technology | メタノールの製造方法及びその製造装置 |
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MX2017017038A (es) | 2018-03-06 |
ES2764150T3 (es) | 2020-06-02 |
EA034976B1 (ru) | 2020-04-14 |
JP6846364B2 (ja) | 2021-03-24 |
US20160368848A1 (en) | 2016-12-22 |
KR102336488B1 (ko) | 2021-12-07 |
EA201890033A1 (ru) | 2018-05-31 |
US10364204B2 (en) | 2019-07-30 |
MY182154A (en) | 2021-01-18 |
WO2016209831A1 (en) | 2016-12-29 |
EP3310747B1 (en) | 2019-11-20 |
BR112017027711A2 (pt) | 2018-09-11 |
KR20180020209A (ko) | 2018-02-27 |
BR112017027711B1 (pt) | 2021-11-23 |
CA2990185A1 (en) | 2016-12-29 |
CN107771172A (zh) | 2018-03-06 |
EP3310747A1 (en) | 2018-04-25 |
CA2990185C (en) | 2023-01-03 |
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