JPWO2020169809A5 - - Google Patents

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JPWO2020169809A5
JPWO2020169809A5 JP2021549266A JP2021549266A JPWO2020169809A5 JP WO2020169809 A5 JPWO2020169809 A5 JP WO2020169809A5 JP 2021549266 A JP2021549266 A JP 2021549266A JP 2021549266 A JP2021549266 A JP 2021549266A JP WO2020169809 A5 JPWO2020169809 A5 JP WO2020169809A5
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Prior art keywords
particulate carbon
carbon material
benzo
process step
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JP2021549266A
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JP2022531753A (en
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Priority claimed from PCT/EP2020/054636 external-priority patent/WO2020169809A2/en
Publication of JP2022531753A publication Critical patent/JP2022531753A/en
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Claims (21)

臭気が低減された微粒子状炭素材料の製造方法であって、
液体に全部又は一部が溶解された出発原料の析出によって得られる微粒子状炭素材料が準備される第1のプロセス工程と
該微粒子状炭素材料が、続いてガス雰囲気中で加熱されることによって第2のプロセス工程で処理され、それによって臭気低減微粒子状炭素材料が得られ、
第2のプロセス工程において、プロセス温度は最高温度が300℃を超えず、最低温度が150℃を下回らず、
第2のプロセス工程におけるガス雰囲気が、
a)15容積%未満の酸素含有量を有する不活性ガスにより富化された空気、および/または
b)500mbar未満の圧力である減圧空気、
から選択される、方法。
A method for producing a particulate carbon material with reduced odor, comprising:
a first process step in which a particulate carbon material obtained by precipitation of a starting material dissolved wholly or partially in a liquid is provided;
the particulate carbon material is subsequently treated in a second process step by heating in a gas atmosphere, thereby obtaining an odor reducing particulate carbon material;
in the second process step, the process temperature does not exceed a maximum temperature of 300°C and a minimum temperature of no less than 150°C;
The gas atmosphere in the second process step is
a) air enriched with inert gas with an oxygen content of less than 15% by volume, and/or
b) decompressed air at a pressure of less than 500 mbar;
A method selected from.
不活性ガスにより富化された空気からなるガス雰囲気の酸素含有量が、少なくとも0.1容積%である、請求項1に記載の方法。 2. A process according to claim 1, wherein the oxygen content of the gas atmosphere consisting of air enriched with inert gas is at least 0.1% by volume. 第1のプロセス工程において、出発原料が50%以上のリグニンを含み、出発原料の析出が、酸性ガスの導入および/または酸を添加することにより起こる、請求項1または2に記載の方法。 3. Process according to claim 1 or 2, wherein in the first process step the starting material contains 50% or more lignin and precipitation of the starting material occurs by introducing acid gas and/or adding acid. 前記第1のプロセス工程において、出発原料が50%以上のリグニンを含み、出発材料の安定化が水熱炭化条件で行われる、請求項1~3のいずれか1項に記載の方法。 Process according to any one of claims 1 to 3 , wherein in the first process step the starting material contains 50% or more lignin and the stabilization of the starting material is carried out under hydrothermal carbonization conditions. 前記微粒子状炭素材料は、前記第1のプロセス工程の後に、少なくとも5m/g以上200m /g以下のBET表面積を有する、請求項1~4のいずれか1項に記載の方法。 The method of any one of claims 1-4 , wherein the particulate carbon material has a BET surface area of at least 5 m 2 /g to 200 m 2 / g after the first process step. 前記第2のプロセス工程の間、微粒子状炭素材料のガス雰囲気下におけるプロセス温度が1秒以上60分未満維持される、請求項1~5のいずれか1項に記載の方法。 The method according to any one of claims 1 to 5, wherein the process temperature of the particulate carbon material under the gas atmosphere is maintained for 1 second or more and 60 minutes or more during the second process step. 第2のプロセス工程において、微粒子状炭素材料がプロセス温度でガス雰囲気下で処理され、さらに該ガス雰囲気下で加熱と冷却が行われる、請求項1~6のいずれか1項に記載の方法。 A method according to any one of the preceding claims, wherein in the second process step the particulate carbon material is treated at a process temperature under a gas atmosphere and further heated and cooled under said gas atmosphere . 前記第2のプロセス工程が、ロータリーキルン中または流動床中で行われる、請求項1~7のいずれか1項に記載の方法。 Process according to any one of the preceding claims, wherein said second process step is carried out in a rotary kiln or in a fluidized bed . 前記第2のプロセス工程が研削または分級と組み合わせて行われる、請求項1~8のいずれか1項に記載の方法。 A method according to any one of the preceding claims, wherein said second process step is performed in combination with grinding or classifying . 前記第1のプロセス工程において、50%を超える糖、デンプン、またはリグニンを含む出発原料から微粒子状炭素材料が得られる、請求項1~9のいずれか1項に記載の方法。A method according to any one of the preceding claims, wherein in said first process step the particulate carbon material is obtained from a starting material containing more than 50% sugars, starches or lignin. 不活性ガスが、窒素、二酸化炭素、過熱水蒸気および前記第2のプロセス工程中に放出されるガス、および/または、不活性ガスによって富化された10容積%未満の酸素濃度を有する空気、からなる群から選択される、請求項1~10のいずれか1項に記載の方法。The inert gas is nitrogen, carbon dioxide, superheated steam and gases released during said second process step, and/or air enriched with inert gas and having an oxygen concentration of less than 10% by volume. A method according to any one of claims 1 to 10, selected from the group consisting of: 請求項1~11のいずれか1項に記載の方法によって得られる、臭気が低減された微粒子状炭素材料。A particulate carbon material with reduced odor obtained by the method according to any one of claims 1-11. ジメチルスルフィドおよびグアヤコールの含有量が1mg/kg未満である、請求項12に記載の、または請求項1~11のいずれか1項に記載の方法により得られた、臭気が低減された微粒子状炭素材料。 Particulate carbon with reduced odor according to claim 12 or obtained by the process according to any one of claims 1 to 11, wherein the content of dimethyl sulfide and guaiacol is less than 1 mg/kg material. ナフタレン含有量が5mg/kg未満である、請求項12または13に記載の、または請求項1~11のいずれか1項に記載の方法により得られた、臭気が低減された微粒子状炭素材料。 A particulate carbon material with reduced odor according to claim 12 or 13 or obtained by the method according to any one of claims 1 to 11, wherein the naphthalene content is less than 5 mg/kg. BGを除く18EPA-PAK(DIN EN16181:2017-11/ドラフトによる)の含有量が5mg/kg未満である、請求項12~14のいずれか1項に記載の、または請求項1~11のいずれか1項に記載の方法により得られた、臭気が低減された微粒子状炭素材料。 12-14 or any one of claims 1-11, wherein the content of 18EPA-PAK excluding BG (according to DIN EN 16181:2017-11/draft) is less than 5 mg/kg 2. A particulate carbon material with reduced odor, obtained by the method according to claim 1. ベンゾ(a)アントラセン、クリセン、ベンゾ(b)フルオロアンテン、ベンゾ(k)フルオロアンテン、ベンゾ(a)ピレン、インデノール(1,2,3-cd)ピレン、ジベンゾル(a,h)アントラセン、ベンゼン(g,h,i)ペリレン、ベンゾ(e)ピレンおよびベンゾ(j)フルオロアンテンの含有量が0.1mg/kg未満である、請求項12~15のいずれか1項に記載の、または請求項1~11のいずれか1項に記載の方法により得られた、臭気が低減された微粒子状炭素材料。 benzo(a)anthracene, chrysene, benzo(b)fluoroantene, benzo(k)fluoroantene, benzo(a)pyrene, indenol(1,2,3-cd)pyrene, dibenzol(a,h)anthracene, benzene ( 16. or according to any one of claims 12 to 15 , wherein the content of g,h,i) perylenes, benzo(e)pyrenes and benzo(j)fluoroantenes is less than 0.1 mg/kg. A particulate carbon material with reduced odor, obtained by the method according to any one of 1 to 11. 請求項12~16のいずれか1項に記載の、または請求項1~11のいずれか1項に記載の方法によって得られる臭気が低減された微粒子状炭素材料の、ポリマーブレンド、特にエラストマーブレンド中の添加剤としての使用。 Particulate carbon material with reduced odor according to any one of claims 12 to 16 or obtained by the process according to any one of claims 1 to 11 in polymer blends, especially elastomer blends. as an additive for 請求項12~16のいずれか1項に規定された臭気が低減された微粒子状炭素材料を含む、ポリマーブレンド。A polymer blend comprising a reduced odor particulate carbon material as defined in any one of claims 12-16. 前記ポリマーブレンドがエラストマーブレンドである、請求項18に記載のポリマーブレンド。19. The polymer blend of claim 18, wherein said polymer blend is an elastomer blend. a)BET表面積が少なくとも5ma) a BET surface area of at least 5m 2 /g、/ g,
b)ジメチルスルフィドおよびグアヤコールの含有量が1mg/kg未満、b) a dimethyl sulfide and guaiacol content of less than 1 mg/kg;
c)STSA表面積からの偏移が最大20%であるBET表面積、c) a BET surface area that deviates up to 20% from the STSA surface area;
d)灰を含まない乾燥物質を基準として、炭素含有量が50~80質量%であり、d) has a carbon content of 50 to 80% by weight, based on ash-free dry matter;
e)ベンゾ(a)アントラセン、クリセン、ベンゾ(b)フルオロアンテン、ベンゾ(k)フルオロアンテン、ベンゾ(a)ピレン、インデノール(1,2,3-cd)ピレン、ジベンゾル(a,h)アントラセン、ベンゼン(g,h,i)ペリレン、ベンゾ(e)ピレンおよびベンゾ(j)フルオロアンテンの含有量が0.1mg/kg未満である、e) benzo(a)anthracene, chrysene, benzo(b)fluoroantene, benzo(k)fluoroantene, benzo(a)pyrene, indenol(1,2,3-cd)pyrene, dibenzol(a,h)anthracene, the content of benzene (g,h,i) perylene, benzo (e) pyrene and benzo (j) fluoroantene is less than 0.1 mg/kg;
再生可能な原材料を基礎とする出発原料から製造された臭気が低減された微粒子状炭素材料。A particulate carbon material with reduced odor produced from renewable raw material-based starting materials.
請求項20に記載の臭気が低減された微粒子状炭素材料を含む、ポリマーブレンド。21. A polymer blend comprising the reduced odor particulate carbon material of claim 20.
JP2021549266A 2019-02-21 2020-02-21 How to reduce the odor of particulate carbon material Pending JP2022531753A (en)

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DE102019104406 2019-02-21
PCT/EP2020/054636 WO2020169809A2 (en) 2019-02-21 2020-02-21 Method for reducing the odour in particle-forming carbon materials

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JPWO2020169809A5 true JPWO2020169809A5 (en) 2022-08-22

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US (1) US20220135408A1 (en)
EP (1) EP3927881A2 (en)
JP (1) JP2022531753A (en)
KR (1) KR20210132058A (en)
CN (1) CN113498424A (en)
BR (1) BR112021015310A2 (en)
CA (1) CA3131170A1 (en)
CL (1) CL2021002011A1 (en)
MX (1) MX2021010141A (en)
WO (1) WO2020169809A2 (en)

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* Cited by examiner, † Cited by third party
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SE543477C2 (en) * 2018-09-07 2021-03-02 Valmet Oy Method of producing lignin with reduced amount of odorous substances
WO2023052365A1 (en) * 2021-09-28 2023-04-06 Suncoal Industries Gmbh Sulfur-crosslinkable rubber composition containing organic fillers and organosilane

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SE0402201D0 (en) 2004-09-14 2004-09-14 Stfi Packforsk Ab Method for separating lignin from black liquor
SE0402437D0 (en) 2004-10-07 2004-10-07 Stfi Packforsk Ab Method for separating lignin from a lignin containing liquid / slurry
DE102006057566B4 (en) * 2006-11-30 2011-02-24 Sächsisches Institut für Angewandte Biotechnologie e.V. (SIAB) Process for producing a low-emission lignocellulosic raw material or material, component or product
US9382389B2 (en) 2008-02-21 2016-07-05 Valmet Aktiebolag Method for separating lignin from black liquor, a lignin product, and use of a lignin product for the production of fuels or materials
BRPI0920883A2 (en) * 2008-10-16 2015-12-22 Evonik Carbon Black Gmbh c-14 high carbon black, its production processes and uses, polymer blends, rubbers and plastics, inks and printing inks comprising such carbon black, and use of such rubber blends.
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FI126849B (en) * 2012-12-19 2017-06-15 Teknologian Tutkimuskeskus Vtt Oy Procedure for hydrothermal treatment of high molecular weight biomaterials
DE102013001678A1 (en) 2013-01-31 2014-07-31 INNOLYSIA GbR (vertretungsberechtigte Gesellschafterin: Virginie Soua, 53639 Königswinter) Method for treating timber used for oriented strand board, paper and cellulose, involves crushing timber products and treating timber with solution of oxidant and inert organic solvent in presence of water and carbon dioxide
DE102014215807B3 (en) 2014-08-08 2015-12-24 Suncoal Industries Gmbh Process for obtaining a stabilized lignin with a defined grain size distribution from a lignin-containing liquid
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