JP2016117678A5 - - Google Patents

Download PDF

Info

Publication number
JP2016117678A5
JP2016117678A5 JP2014257897A JP2014257897A JP2016117678A5 JP 2016117678 A5 JP2016117678 A5 JP 2016117678A5 JP 2014257897 A JP2014257897 A JP 2014257897A JP 2014257897 A JP2014257897 A JP 2014257897A JP 2016117678 A5 JP2016117678 A5 JP 2016117678A5
Authority
JP
Japan
Prior art keywords
furfural
compound
composition
furan
producing
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.)
Pending
Application number
JP2014257897A
Other languages
Japanese (ja)
Other versions
JP2016117678A (en
Filing date
Publication date
Application filed filed Critical
Priority to JP2014257897A priority Critical patent/JP2016117678A/en
Priority claimed from JP2014257897A external-priority patent/JP2016117678A/en
Publication of JP2016117678A publication Critical patent/JP2016117678A/en
Publication of JP2016117678A5 publication Critical patent/JP2016117678A5/ja
Pending legal-status Critical Current

Links

Description

即ち、本発明の要旨は、以下の[1]〜[7]に存する。
[1]原料としてフルフラール化合物を主成分として含むフルフラール組成物を反応器に
供給し、触媒の存在下で脱カルボニル化反応を行うことによりフラン化合物を製造する際
、該フルフラール組成物中の2−アセチルフラン濃度が120重量ppm以上2000重
量ppm以下であることを特徴とするフラン化合物の製造方法。
[2] 前記原料のフルフラール組成物のフルフラール化合物の濃度が99.00重量%
〜99.95重量%である[1]に記載のフラン化合物の製造方法。
[3]前記触媒が、担体がジルコニアで、且つ担持金属がパラジウムを含む固体触媒であ
ることを特徴とする[1]又は[2]に記載のフラン化合物の製造方法。
[4]前記フルフラール組成物中の前記フルフラール化合物がフルフラールであって、以
下の工程(a)を更に有することを特徴とする上記[1]〜[3]のいずれか1に記載の
フラン化合物の製造方法。
(a) 粗フルフラールと陰イオン交換樹脂及び/又は塩基性化合物を接触させた後に、
得られる粗フルフラールを蒸留塔で蒸留し、フルフラールよりも高い沸点を有する化合物
及び/又はフルフラールよりも低い沸点を有する化合物を除去して、フルフラール組成物
を製造する工程
[5][1]〜[4]のいずれか1に記載のフラン化合物の製造方法により得られるフラン
を触媒の存在下で水素化反応を行うことによりテトラヒドロフランを製造する、テトラヒ
ドロフランの製造方法。
[6]フルフラール化合物を主成分として含むフルフラール組成物であって、該組成物中
の2−アセチルフランの濃度が120重量ppm以上2000重量ppm以下である、フ
ルフラール組成物。
[7]前記フルフラール化合物の濃度が99.00重量%〜99.95重量%である[6
]に記載のフルフラール組成物。
That is, the gist of the present invention resides in the following [1] to [7].
[1] When producing a furan compound by supplying a furfural composition containing a furfural compound as a main component as a raw material to a reactor and performing a decarbonylation reaction in the presence of a catalyst, A method for producing a furan compound, wherein the acetylfuran concentration is 120 ppm by weight or more and 2000 ppm by weight or less.
[2] The concentration of the furfural compound in the raw furfural composition is 99.00% by weight.
The manufacturing method of the furan compound as described in [1] which is -99.95 weight%.
[3] The method for producing a furan compound according to [1] or [2], wherein the catalyst is a solid catalyst in which the carrier is zirconia and the supported metal includes palladium.
[4] The furfural compound in any one of the above [1] to [3], wherein the furfural compound in the furfural composition is furfural and further includes the following step (a): Production method.
(A) After contacting the crude furfural with an anion exchange resin and / or a basic compound,
The obtained crude furfural is distilled in a distillation column, and a compound having a boiling point higher than that of furfural and / or a compound having a boiling point lower than that of furfural is removed to produce a furfural composition [5] [1] to [ 4] A method for producing tetrahydrofuran, wherein tetrahydrofuran is produced by hydrogenating a furan obtained by the method for producing a furan compound according to any one of 4) in the presence of a catalyst.
[6] A furfural composition comprising a furfural compound as a main component, wherein the concentration of 2-acetylfuran in the composition is 120 ppm to 2000 ppm by weight.
[7] The concentration of the furfural compound is 99.00 wt% to 99.95 wt% [6]
] The furfural composition as described in above.

Claims (7)

原料としてフルフラール化合物を主成分として含むフルフラール組成物を反応器に供給
し、触媒の存在下で脱カルボニル化反応を行うことによりフラン化合物を製造する際、該
フルフラール組成物中の2−アセチルフラン濃度が120重量ppm以上2000重量p
pm以下であることを特徴とするフラン化合物の製造方法。
When producing a furan compound by supplying a furfural composition containing a furfural compound as a main component as a raw material to a reactor and performing a decarbonylation reaction in the presence of a catalyst, the concentration of 2-acetylfuran in the furfural composition Is 120ppm by weight or more and 2000wtp
The manufacturing method of the furan compound characterized by being below pm.
前記原料のフルフラール組成物のフルフラール化合物の濃度が99.00重量%〜99
.95重量%である請求項1に記載のフラン化合物の製造方法。
The concentration of the furfural compound in the raw furfural composition is 99.00% by weight to 99%.
. The method for producing a furan compound according to claim 1, which is 95% by weight.
前記触媒が、担体がジルコニアで、且つ担持金属がパラジウムを含む固体触媒であるこ
とを特徴とする請求項1又は2に記載のフラン化合物の製造方法。
The method for producing a furan compound according to claim 1 or 2, wherein the catalyst is a solid catalyst in which the carrier is zirconia and the supported metal contains palladium.
前記フルフラール組成物中の前記フルフラール化合物がフルフラールであって、以下の
工程(a)を更に有することを特徴とする請求項1〜3のいずれか1項に記載のフラン化
合物の製造方法。
(a) 粗フルフラールと陰イオン交換樹脂及び/又は塩基性化合物を接触させた後に、
得られる粗フルフラールを蒸留塔で蒸留し、フルフラールよりも高い沸点を有する化合物
及び/又はフルフラールよりも低い沸点を有する化合物を除去して、フルフラール組成物
を製造する工程
The said furfural compound in the said furfural composition is a furfural, Comprising: It further has the following process (a), The manufacturing method of the furan compound of any one of Claims 1-3 characterized by the above-mentioned.
(A) After contacting the crude furfural with an anion exchange resin and / or a basic compound,
A step of producing a furfural composition by distilling the resulting crude furfural in a distillation column and removing a compound having a boiling point higher than that of furfural and / or a compound having a boiling point lower than that of furfural.
請求項1〜4のいずれか1項に記載のフラン化合物の製造方法により得られるフランを
触媒の存在下で水素化反応を行うことによりテトラヒドロフランを製造する、テトラヒド
ロフランの製造方法。
The manufacturing method of tetrahydrofuran which manufactures tetrahydrofuran by hydrogenating the furan obtained by the manufacturing method of the furan compound of any one of Claims 1-4 in presence of a catalyst.
フルフラール化合物を主成分として含むフルフラール組成物であって、該組成物中の2
−アセチルフランの濃度が120重量ppm以上2000重量ppm以下である、フルフ
ラール組成物。
A furfural composition comprising a furfural compound as a main component, wherein 2 in the composition
-The furfural composition whose concentration of acetyl furan is 120 weight ppm or more and 2000 weight ppm or less.
前記フルフラール化合物の濃度が99.00重量%〜99.95重量%である請求項6
に記載のフルフラール組成物。
The concentration of the furfural compound is 99.00 wt% to 99.95 wt%.
A furfural composition as described in 1. above.
JP2014257897A 2014-12-19 2014-12-19 Manufacturing method of furan compound and manufacturing method of tetrahydrofuran Pending JP2016117678A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2014257897A JP2016117678A (en) 2014-12-19 2014-12-19 Manufacturing method of furan compound and manufacturing method of tetrahydrofuran

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2014257897A JP2016117678A (en) 2014-12-19 2014-12-19 Manufacturing method of furan compound and manufacturing method of tetrahydrofuran

Publications (2)

Publication Number Publication Date
JP2016117678A JP2016117678A (en) 2016-06-30
JP2016117678A5 true JP2016117678A5 (en) 2017-10-19

Family

ID=56243719

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2014257897A Pending JP2016117678A (en) 2014-12-19 2014-12-19 Manufacturing method of furan compound and manufacturing method of tetrahydrofuran

Country Status (1)

Country Link
JP (1) JP2016117678A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111548333B (en) * 2020-05-28 2022-08-30 陕西延长石油(集团)有限责任公司 Method for preparing delta-valerolactone

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5315679B2 (en) * 2007-11-30 2013-10-16 三菱化学株式会社 Method for producing furan compound
JP5375054B2 (en) * 2007-11-30 2013-12-25 三菱化学株式会社 Method for producing furan compound
AU2009327449B2 (en) * 2008-12-18 2015-12-24 Covation Inc. Vapor phase decarbonylation process
BRPI0914400A2 (en) * 2008-12-18 2015-08-04 Du Pont "process for the synthesis of a compound"
BR112012004397B1 (en) * 2009-08-31 2021-03-30 E.I. Du Pont De Nemours And Company PROCESS TO SYNTHESIZE A COMPOUND
AU2010286449B2 (en) * 2009-08-31 2016-06-23 Covation Inc. Vapor phase decarbonylation process
US8653287B2 (en) * 2009-08-31 2014-02-18 E I Du Pont De Nemours And Company Decarbonylation process
JP5948921B2 (en) * 2012-02-08 2016-07-06 三菱化学株式会社 Production method of furan
JP6299086B2 (en) * 2012-06-08 2018-03-28 三菱ケミカル株式会社 Method for purifying furfural
JP2013253061A (en) * 2012-06-08 2013-12-19 Mitsubishi Chemicals Corp Method for purifying furfural and method for producing furan
US9333493B2 (en) * 2012-10-23 2016-05-10 Shell Oil Company Regeneration of aldehyde decarbonylation catalysts
US9650354B2 (en) * 2013-06-25 2017-05-16 Council Of Scientific & Industrial Research Process for producing furan and its derivatives
JP2015140311A (en) * 2014-01-28 2015-08-03 国立大学法人九州大学 Method for producing furan compound
JP6575126B2 (en) * 2014-05-08 2019-09-18 三菱ケミカル株式会社 Method for producing furfural and method for producing furan

Similar Documents

Publication Publication Date Title
SA113340200B1 (en) Process for production of hexamethylenediamine from 5- hydroxymethylfurfural
MY168412A (en) Method for producing substituted 5-fluoro-1h-pyrazolopyridines
BR112017005850A2 (en) process and apparatus for preparing a terephthalic diester.
RU2013148092A (en) METHOD FOR CLEANING PROPYLENE OXIDE
PH12015500327B1 (en) Hydrogen catalyst and process for production thereof by the use of uncalcined starting material
MY150056A (en) Method for producing hydrogenolysis product of polyhydric alcohol
JP2011001364A5 (en)
JP2014528463A5 (en)
FR2979344B1 (en) PROCESS FOR THE PREPARATION OF FURFURAL
MY181657A (en) Catalyst for hydrogenolysis of polyhydric alcohol and method for producing 1,3-propanediol using catalyst for hydrogenolysis of polyhydric alcohol
JP2018021011A5 (en)
JP2016117678A5 (en)
JP6299086B2 (en) Method for purifying furfural
WO2012149156A3 (en) Process to reduce ethanol recycled to acetic acid hydrogenation reactor
WO2016055456A3 (en) Production of an aromatic dicarboxylic acid
WO2016093592A3 (en) Method for preparing polyalkylene carbonate resin
BR112013010554A2 (en) Method for the preparation of 1,3,5-trioxane
JP2018153140A5 (en)
WO2016207711A8 (en) Modified lignin, epoxy resin, and method for producing same
WO2012103170A3 (en) Tin(ii) 2-hydroxycarboxylates
JP2016527363A5 (en)
MX2015005343A (en) Pure plant mother liquor solvent extraction system and method.
TH147176A (en) Methods for the production of tetrahydrofuran
MY187598A (en) Method for producing hydrocarbon oil
WO2017204554A3 (en) Method for preparing silane derivatives from furan derivatives in presence of borane catalyst