SI20745B - Postopek proizvodnje furfurala - Google Patents
Postopek proizvodnje furfurala Download PDFInfo
- Publication number
- SI20745B SI20745B SI200020014A SI200020014A SI20745B SI 20745 B SI20745 B SI 20745B SI 200020014 A SI200020014 A SI 200020014A SI 200020014 A SI200020014 A SI 200020014A SI 20745 B SI20745 B SI 20745B
- Authority
- SI
- Slovenia
- Prior art keywords
- process according
- furfural
- predetermined temperature
- steam
- reached
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
- C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
- C07D307/34—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
- C07D307/38—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with substituted hydrocarbon radicals attached to ring carbon atoms
- C07D307/40—Radicals substituted by oxygen atoms
- C07D307/46—Doubly bound oxygen atoms, or two oxygen atoms singly bound to the same carbon atom
- C07D307/48—Furfural
- C07D307/50—Preparation from natural products
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Furan Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
V novem postopku proizvodnje furfurala segrevamo surovino, ki vsebuje pentosan in je okisana ali ne, do temperature T1, z dovajanjem pare skozi ventil (2), medtem, ko sta ventila (3, 4) zaprta. Po zelo kratkem postopku segrevanja, para kondenzira in tako poveča vsebnost vlage polnila. Nato ventil (2) zapremo in odpremo izpustni ventil (3), da nastane stalen majhen pretok pare produkta s postopnim zmanjševanjem tlaka. To povzroči počasen padec temperature. Ko tako dosežemo primerno določeno temperaturo T2, izpustni ventil (3) zapremo in tako zaključimo prvo postopno zmanjševanje tlaka. Če ob koncu tega ciklusa ne moremo dobiti nič več furfurala, postopek zaključimo tako, da odpremo ventil (4) in iz posode izpraznimo ostanek. Če pa furfural lahko pridobivamo še naprej, reaktor ponovno segrejemo in pričnemo nov ciklus postopnega zmanjševanja tlaka.
Claims (10)
1 PATENTNI ZAHTEVKI 1. Postopek proizvodnje furfurala, značilen po tem, da obsega naslednje korake: - polnjenje reaktorja z materialom, ki vsebuje pentosan, segrevanje polnitve z uvajanjem pare pod tlakom do prve. vnaprej določene temperature, ki ni višja od 250°C. zapiranje ventila za uvajanje pare in izpostavljanja polnitve postopnemu zmanjševanju tlaka, dokler ne dosežemo druge vnaprej določene temperature, ki ni nižja od 150°C, kjer je stopnja zmanjševanje tlaka takšna, da tekoča faza v reaktorju ves čas vre in je omenjena stopnja dovolj visoka, za celotno pretvorbo v furfural preden je dosežena druga vnaprej določena temperatura.
2. Postopek po zahtevku 1, značilen po tem, da je polnilo pred gretjem okisano.
3. Postopek po zahtevku 1, značilen po tem, da je stopnja zmanjševanja tlaka dovolj velika, da se zaključi pretvorba v furfural preden dosežemo drugo vnaprej določeno temperaturo.
4. Postopek po zahtevku 1, značilen po tem, da pretvorbo v furfural dosežemo v več kot enem ciklusu zmanjševanja tlaka od prve vnaprej določene temperature do druge vnaprej določene temperature z dodajanjem pare.
Postopek po zahtevku 1, značilen po tem, da med zmanjševanjem tlaka, določen čas dodajamo paro.
6. Postopek po zahtevku 1, značilen po tem, da postopno zmanjševanje tlaka obsega nadzorovanje izpuščanje pare iz reakcije, dokler ne dosežemo druge vnaprej določene temperature.
7. Postopek po zahtevku L značilen po tem, da se postopno zmanjševanje tlaka odvija v temperaturnem obsegu med 280°C in 150°C. z
8. Postopek po zahtevku 7, značilen po tem. daje temperaturni obseg delovanja med 230° in 170°C.
9. Postopek po zahtevku 1. značilen po tem, da kot katalizator uporabimo fosforno kislino.
10. Postopek po zahtevku 1, značilen po tem, da kot dodani katalizator uporabimo ocetno kislino.
Mark - Inventa za
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19905655A DE19905655A1 (de) | 1999-02-11 | 1999-02-11 | Verfahren zur Herstellung von Furfural durch verzögerte Entspannung |
PCT/ZA2000/000024 WO2000047569A1 (en) | 1999-02-11 | 2000-02-11 | Process for the manufacture of furfural |
Publications (2)
Publication Number | Publication Date |
---|---|
SI20745A SI20745A (sl) | 2002-06-30 |
SI20745B true SI20745B (sl) | 2009-04-30 |
Family
ID=7897146
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SI200020014A SI20745B (sl) | 1999-02-11 | 2000-02-11 | Postopek proizvodnje furfurala |
Country Status (16)
Country | Link |
---|---|
US (1) | US6743928B1 (sl) |
EP (1) | EP1161426B1 (sl) |
AP (1) | AP1391A (sl) |
AT (1) | ATE363476T1 (sl) |
AU (1) | AU772210B2 (sl) |
BR (1) | BR0008143A (sl) |
CY (1) | CY1107723T1 (sl) |
DE (2) | DE19905655A1 (sl) |
DK (1) | DK1161426T3 (sl) |
ES (1) | ES2290021T3 (sl) |
MX (1) | MXPA01008096A (sl) |
PT (1) | PT1161426E (sl) |
SI (1) | SI20745B (sl) |
TR (1) | TR200102691T2 (sl) |
WO (1) | WO2000047569A1 (sl) |
ZA (1) | ZA200106721B (sl) |
Families Citing this family (43)
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FI117633B (fi) * | 2000-12-29 | 2006-12-29 | Chempolis Oy | Kemikaalien talteenotto ja valmistus massan valmistuksen yhteydessä |
EP2032550B1 (en) | 2006-06-06 | 2013-11-20 | Wisconsin Alumni Research Foundation | Catalytic process for producing furan derivatives from carbohydrates in a biphasic reactor |
US8282738B2 (en) * | 2008-07-16 | 2012-10-09 | Renmatix, Inc. | Solvo-thermal fractionation of biomass |
US8119823B2 (en) * | 2008-07-16 | 2012-02-21 | Renmatix, Inc. | Solvo-thermal hydrolysis of xylose |
CA2730766C (en) * | 2008-07-16 | 2016-11-01 | Sriya Innovations, Inc. | Method of extraction of furfural and glucose from biomass using one or more supercritical fluids |
US8546560B2 (en) * | 2008-07-16 | 2013-10-01 | Renmatix, Inc. | Solvo-thermal hydrolysis of cellulose |
CA2638150C (en) | 2008-07-24 | 2012-03-27 | Sunopta Bioprocess Inc. | Method and apparatus for conveying a cellulosic feedstock |
CA2638159C (en) | 2008-07-24 | 2012-09-11 | Sunopta Bioprocess Inc. | Method and apparatus for treating a cellulosic feedstock |
CA2638157C (en) | 2008-07-24 | 2013-05-28 | Sunopta Bioprocess Inc. | Method and apparatus for conveying a cellulosic feedstock |
CA2650919C (en) | 2009-01-23 | 2014-04-22 | Sunopta Bioprocess Inc. | Method and apparatus for conveying a cellulosic feedstock |
US8915644B2 (en) | 2008-07-24 | 2014-12-23 | Abengoa Bioenergy New Technologies, Llc. | Method and apparatus for conveying a cellulosic feedstock |
CA2650913C (en) | 2009-01-23 | 2013-10-15 | Sunopta Bioprocess Inc. | Method and apparatus for conveying a cellulosic feedstock |
US9127325B2 (en) | 2008-07-24 | 2015-09-08 | Abengoa Bioenergy New Technologies, Llc. | Method and apparatus for treating a cellulosic feedstock |
CA2638160C (en) | 2008-07-24 | 2015-02-17 | Sunopta Bioprocess Inc. | Method and apparatus for conveying a cellulosic feedstock |
US8669397B2 (en) | 2009-06-13 | 2014-03-11 | Rennovia, Inc. | Production of adipic acid and derivatives from carbohydrate-containing materials |
CN102803194B (zh) | 2009-06-13 | 2016-01-20 | 莱诺维亚公司 | 由含碳水化合物的物质生产戊二酸和衍生物 |
CA2763777C (en) | 2009-06-13 | 2017-10-17 | Rennovia Inc. | Production of adipic acid and derivatives from carbohydrate-containing materials |
CA2755981C (en) | 2009-08-24 | 2015-11-03 | Abengoa Bioenergy New Technologies, Inc. | Method for producing ethanol and co-products from cellulosic biomass |
CN112159869B (zh) | 2010-01-19 | 2024-04-19 | 瑞恩麦特克斯股份有限公司 | 使用超临界流体从生物质产生可发酵的糖和木质素 |
US8669393B2 (en) | 2010-03-05 | 2014-03-11 | Rennovia, Inc. | Adipic acid compositions |
US9770705B2 (en) | 2010-06-11 | 2017-09-26 | Rennovia Inc. | Oxidation catalysts |
CN103270028B (zh) | 2010-12-21 | 2015-11-25 | 纳幕尔杜邦公司 | 由釜馏物或糖浆中的支链不可发酵糖制备糠醛的方法 |
SG194724A1 (en) | 2011-05-04 | 2013-12-30 | Renmatix Inc | Lignin production from lignocellulosic biomass |
US8801859B2 (en) | 2011-05-04 | 2014-08-12 | Renmatix, Inc. | Self-cleaning apparatus and method for thick slurry pressure control |
US8389749B2 (en) | 2011-05-25 | 2013-03-05 | Wisconsin Alumni Research Foundation | Method to produce, recover and convert furan derivatives from aqueous solutions using alkylphenol extraction |
WO2013025564A2 (en) * | 2011-08-12 | 2013-02-21 | E. I. Du Pont De Nemours And Company | Furfural production from biomass |
WO2013102002A1 (en) | 2011-12-28 | 2013-07-04 | E. I. Du Pont De Nemours And Company | Processes for making furfurals |
US9181211B2 (en) | 2011-12-28 | 2015-11-10 | E I Du Pont De Nemours And Company | Process for the production of furfural |
AU2012362300A1 (en) * | 2011-12-28 | 2014-06-26 | E. I. Du Pont De Nemours And Company | Process for the production of furfural |
WO2013102007A1 (en) * | 2011-12-28 | 2013-07-04 | E. I. Du Pont De Nemours And Company | Process for the production of furfural |
CN104024238B (zh) | 2011-12-28 | 2016-07-06 | 纳幕尔杜邦公司 | 用于制备糠醛的方法 |
US8759498B2 (en) | 2011-12-30 | 2014-06-24 | Renmatix, Inc. | Compositions comprising lignin |
BR112014017585B1 (pt) | 2012-01-18 | 2020-11-24 | Archer-Daniels-Midland Company | processo para produção de hexametileno diamina a partir de materiais contendo carboidrato e intermediários para os mesmos |
US9174909B2 (en) | 2012-02-02 | 2015-11-03 | Wisconsin Alumni Research Foundation | Two-stage, acid-catalyzed conversion of carbohydrates into levulinic acid |
CN103193737B (zh) * | 2013-03-29 | 2015-01-28 | 山东龙力生物科技股份有限公司 | 植物材料制备糠醛并联产木质素和纤维乙醇的方法 |
WO2015113060A2 (en) | 2014-01-27 | 2015-07-30 | Rennovia, Inc. | Conversion of fructose-containing feedstocks to hmf-containing product |
CN105143196A (zh) * | 2014-03-07 | 2015-12-09 | 花王株式会社 | 糠醛的制造方法 |
AU2015320328B2 (en) | 2014-09-26 | 2020-03-05 | Renmatix, Inc. | Cellulose-containing compositions and methods of making same |
JP2017537920A (ja) | 2014-12-02 | 2017-12-21 | レノビア インコーポレイテッド | 5−ヒドロキシメチルフルフラールから2,5−ビスヒドロキシメチルフラン、2,5−ビス−ヒドロキシメチルテトラヒドロフラン、1,6−ヘキサンジオールおよび1,2,6−ヘキサントリオールを生成する工程 |
WO2017123763A1 (en) | 2016-01-13 | 2017-07-20 | Rennovia Inc. | Processes for the preparation of 2,5-furandicarboxylic acid and intermediates and derivatives thereof |
EP3652161A1 (en) | 2017-07-12 | 2020-05-20 | Stora Enso Oyj | Purified 2,5-furandicarboxylic acid pathway products |
CN108976184A (zh) * | 2018-09-13 | 2018-12-11 | 山东太阳纸业股份有限公司 | 一种溶解浆木片水解液制造糠醛工艺 |
EP3626711A1 (en) | 2018-09-24 | 2020-03-25 | Arbaflame Technology AS | Process for the production of furfural |
Family Cites Families (8)
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FI51371C (fi) | 1974-10-04 | 1976-12-10 | Rosenlew Ab Oy W | Menetelmä polysakkaridipitoisen raaka-aineen hajottamiseksi happohydro lyysin avulla. |
FR2462433A1 (fr) * | 1979-08-03 | 1981-02-13 | Bertin & Cie | Perfectionnements apportes aux procedes et aux appareillages pour l'obtention de furfural a partir de matieres vegetales |
DE3139188C1 (de) * | 1981-10-02 | 1983-07-28 | Knauth, Hans, Dipl.-Ing., 7758 Meersburg | Verfahren zur Herstellung von Furfurol und Glucose |
US4533743A (en) * | 1983-12-16 | 1985-08-06 | Atlantic Richfield Company | Furfural process |
SU1225841A1 (ru) * | 1983-12-22 | 1986-04-23 | Краснодарский ордена Трудового Красного Знамени политехнический институт | Непрерывный способ получени фурфурола |
DE3842825A1 (de) * | 1988-01-08 | 1989-07-20 | Krupp Gmbh | Verfahren und vorrichtung zur herstellung von furfural |
CS274575B2 (en) * | 1988-06-13 | 1991-08-13 | Reiner Doc Ing Csc Seifert | Method of 2-furaldehyde,cellulose and lignin production from lignocellulosic materials |
CZ281504B6 (cs) * | 1995-02-08 | 1996-10-16 | Zdeněk Kratochvíl | Způsob zpracování lignocelulózových materiálů kontinuální tlakovou hydrolýzou a zařízení |
-
1999
- 1999-02-11 DE DE19905655A patent/DE19905655A1/de not_active Withdrawn
-
2000
- 2000-02-11 AP APAP/P/2001/002263A patent/AP1391A/en active
- 2000-02-11 MX MXPA01008096A patent/MXPA01008096A/es active IP Right Grant
- 2000-02-11 DK DK00912231T patent/DK1161426T3/da active
- 2000-02-11 DE DE60035029T patent/DE60035029T2/de not_active Expired - Lifetime
- 2000-02-11 US US09/913,280 patent/US6743928B1/en not_active Expired - Fee Related
- 2000-02-11 PT PT00912231T patent/PT1161426E/pt unknown
- 2000-02-11 TR TR2001/02691T patent/TR200102691T2/xx unknown
- 2000-02-11 SI SI200020014A patent/SI20745B/sl not_active IP Right Cessation
- 2000-02-11 AU AU33991/00A patent/AU772210B2/en not_active Ceased
- 2000-02-11 ES ES00912231T patent/ES2290021T3/es not_active Expired - Lifetime
- 2000-02-11 BR BR0008143-4A patent/BR0008143A/pt not_active Application Discontinuation
- 2000-02-11 AT AT00912231T patent/ATE363476T1/de active
- 2000-02-11 WO PCT/ZA2000/000024 patent/WO2000047569A1/en active IP Right Grant
- 2000-02-11 EP EP00912231A patent/EP1161426B1/en not_active Expired - Lifetime
-
2001
- 2001-08-15 ZA ZA200106721A patent/ZA200106721B/xx unknown
-
2007
- 2007-08-28 CY CY20071101132T patent/CY1107723T1/el unknown
Also Published As
Publication number | Publication date |
---|---|
DE19905655A1 (de) | 2000-08-17 |
SI20745A (sl) | 2002-06-30 |
DK1161426T3 (da) | 2007-10-08 |
BR0008143A (pt) | 2002-03-12 |
TR200102691T2 (tr) | 2002-10-21 |
ATE363476T1 (de) | 2007-06-15 |
PT1161426E (pt) | 2007-09-10 |
AU3399100A (en) | 2000-08-29 |
AP1391A (en) | 2005-04-15 |
DE60035029T2 (de) | 2008-01-24 |
EP1161426A1 (en) | 2001-12-12 |
AU772210B2 (en) | 2004-04-22 |
WO2000047569A1 (en) | 2000-08-17 |
EP1161426B1 (en) | 2007-05-30 |
DE60035029D1 (de) | 2007-07-12 |
CY1107723T1 (el) | 2013-04-18 |
MXPA01008096A (es) | 2005-10-05 |
ZA200106721B (en) | 2002-08-26 |
US6743928B1 (en) | 2004-06-01 |
AP2001002263A0 (en) | 2001-09-30 |
ES2290021T3 (es) | 2008-02-16 |
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IF | Valid on the event date | ||
SP73 | Change of data on owner |
Owner name: PROSERPINE CO-OPERATIVE SUGAR MILLING ASSOCIAT; AU Effective date: 20080723 |
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OU02 | Decision according to article 73(2) ipa 1992, publication of decision on partial fulfilment of the invention and change of patent claims |
Effective date: 20090116 |
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Effective date: 20151023 |