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SE466156B - SETTING AND CONSTRUCTION FOR MANUFACTURING ENGINE SPRING OF CELLULOUS WASTE AND WASTE MATERIALS - Google Patents

SETTING AND CONSTRUCTION FOR MANUFACTURING ENGINE SPRING OF CELLULOUS WASTE AND WASTE MATERIALS

Info

Publication number
SE466156B
SE466156B SE8901311A SE8901311A SE466156B SE 466156 B SE466156 B SE 466156B SE 8901311 A SE8901311 A SE 8901311A SE 8901311 A SE8901311 A SE 8901311A SE 466156 B SE466156 B SE 466156B
Authority
SE
Sweden
Prior art keywords
waste
alcohol
paper
plant
materials
Prior art date
Application number
SE8901311A
Other languages
Swedish (sv)
Other versions
SE8901311D0 (en
SE8901311L (en
Inventor
C-O Ranzen
Original Assignee
Erecta Ag
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Erecta Ag filed Critical Erecta Ag
Priority to SE8901311A priority Critical patent/SE466156B/en
Publication of SE8901311D0 publication Critical patent/SE8901311D0/en
Priority to PCT/SE1990/000248 priority patent/WO1990012103A1/en
Priority to AU54498/90A priority patent/AU5449890A/en
Publication of SE8901311L publication Critical patent/SE8901311L/en
Publication of SE466156B publication Critical patent/SE466156B/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • C12P7/08Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate
    • C12P7/10Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate substrate containing cellulosic material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B9/00General arrangement of separating plant, e.g. flow sheets
    • B03B9/06General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Processing Of Solid Wastes (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Description

'Ã66 156 2 10 15 25 30 35 I vissa fall kan det vara fördelaktigt att slamma upp det sön- derdelade papperet till en pumpbar massa, som sedan pumpas till defibreringen, men detta steg är i allmänhet obehövligt. 'Ã66 156 2 10 15 25 30 35 In some cases, it may be beneficial to slurry the divided the paper into a pumpable mass, which is then pumped to defibration, but this step is generally unnecessary.

För defibreringen ger en vanlig skivraffinör ett bra resultat, men en turboraffinör enligt Asplund har visat sig vara särskilt lämplig och ge en mycket bra defibrering.For defibration, an ordinary disk refiner gives a good result, but a turbo refiner according to Asplund has proven to be special suitable and give a very good defibration.

Från defibratorn ledes massan till en tank 6 för att sedan silas 7. Massasilar av olika slag användes inom cellulosaindustrin och de flesta av de vanliga silarna har visat sig användbara. Vid silningen avskiljes större partiklar, en del plastfragment, m.m. som kan ledas tillbaka till defibreringen eller samman med mäsk- resterna gá till brikettering.From the defibrator, the pulp is led to a tank 6 and then filtered 7. Mass screens of various kinds were used in the cellulose industry and most of the standard strainers have proven useful. At the sieve separates larger particles, some plastic fragments, etc. which can be traced back to the defibration or together with the mesh the remains went to briquetting.

Efter koncentrering i en urvattnare 8 ledes massan till en hyd- rolys 9, där cellulosan brytes ned till sockerarter. Hydrolysen kan göras med någon syra, svavelsyra, saltsyra, myrsyra, svavel- dioxid, etc. eller också enzymatiskt. En enzymatisk nedbrytning med'immobiliseradefenzymergharfvisatïsig-fördeïaktigabädêimedä, avseende pà resultat och ekonomi.After concentration in a dewaterer 8, the mass is led to a rolys 9, where the cellulose is broken down into sugars. The hydrolysis can be made with any acid, sulfuric acid, hydrochloric acid, formic acid, sulfuric acid dioxide, etc. or also enzymatically. An enzymatic degradation with the immobilized enzymes that have been shown to be beneficial, both in terms of results and finances.

I en lagringstank lO justeras pH till ett för fermentering lämp- ligt värde genom neutralisering med exempelvis kalk. Fermente- ringen sker i stora jäskar ll där de ingående sockerarterna för- jäses till etanol.In a storage tank 10, the pH is adjusted to a suitable for fermentation. value by neutralization with, for example, lime. Fermented The fermentation takes place in large yeasts where the constituent sugars are fermented to ethanol.

Mäsken renas 12 från fasta beståndsdelar med silar, filter, cen- trifuger eller cykloner och den klarade lösningen ledes till destillation 13.The mash is purified 12 from solids with sieves, filters, centrifuges trifuges or cyclones and the clarified solution is led to distillation 13.

De föroreningar som finns i mäsken stör inte jäsningen, då de till stor del är inerta under de rådande betingelserna, såsom ligninet, fyllmedlen i papperet, kaolin, titanvitt, barytvitt, etc., vaxer, plaster m.m. Vissa plåster kan visserligen lösa sig något i de bildade alkoholerna, men detta har ingen inverkan pà destillationen. 10 15 3 466 156 Mäskresterna fràn klarningen går till en brikettpress l4, där de eventuellt samman med de fasta beståndsdelarna fràn silarna 7 pressas till briketter, som efter torkning kan användas som bränsle. Mängden obrännbara fyllmedel i briketterna beror på den ingående råvaran och kan variera mellan några och flera tiotal procent, men generellt får briketterna ett bra bränslevärde.The contaminants present in the mash do not interfere with the fermentation, as they are largely inert under the prevailing conditions, such as lignin, paper fillers, kaolin, titanium white, barite white, etc., waxes, plasters m.m. Admittedly, some patches can dissolve something in the alcohols formed, but this has no effect on the distillation. 10 15 3 466 156 The mash residues from the clarification go to a briquette press l4, where they possibly together with the solids of the sieves 7 pressed into briquettes, which after drying can be used as fuel. The amount of non-combustible fillers in the briquettes depends on it the raw material included and can vary between a few and several tens percent, but generally the briquettes get a good fuel value.

Eventuellt kan också jäst återvinnas ur mäskresterna.Yeast may also be recovered from the mash residues.

Den avdestillerade etanolen innehåller förutom ett par procent vatten även metanol, högre alkoholer och estrar och den kan an- vändas direkt i motorer eventuellt efter torkning för att minska vattenhalten. Åtminstone en del av återstoden efter destillationen kan ledas tillbaka till fermenteringen ll för ytterligare jäsning eller efterjâsas separat och därefter renas och gå till avloppet.The distilled ethanol contains in addition to a few percent water also methanol, higher alcohols and esters and it can be used turn directly into engines possibly after drying to reduce water content. At least a portion of the residue after distillation can be passed back to the fermentation ll for further fermentation or fermented separately and then cleaned and go to the drain.

Claims (7)

466 156 10 15 20 25 30 35 P a t e n t k r a v466 156 10 15 20 25 30 35 P a t e n t k r a v l. Anläggning för tillverkning av alkohol av pappersavfall och kvittblivning av återstoderna, k ä n n e t e c k n a d av att den består av fragmentator (l) för finfördelning av pappersav- fallet, rensningsanläggning (2) för att avlägsna järn och andra metaller och att sikta det finfördelade materialet, raffinör (5) för defibrering, hydrolysator (9) för nedbrytning av cellulosan till enklare sockerarter, fermentor (ll) för jäsning av de enk- lare sockerarterna till alkohol och en destillationsanläggning (13) för avdestillering av alkoholen.Plant for the production of alcohol from paper waste and disposal of the residues, characterized in that it consists of a fragmentator (l) for atomizing the waste paper, a treatment plant (2) for removing iron and other metals and for sifting the pulverized material , refiner (5) for defibration, hydrolyzer (9) for decomposition of the cellulose into simpler sugars, fermenter (ll) for fermentation of the simpler sugars for alcohol and a distillation plant (13) for distillation of the alcohol. 2. Anläggning enligt krav 1, av si- lar (7, 12) eller andra separatorer efter raffinören (5) och/ eller efter fermentorn (ll). k ä n n e t e c k n a dPlant according to claim 1, of sieves (7, 12) or other separators after the refiner (5) and / or after the fermenter (II). k ä n n e t e c k n a d 3. Anläggning enligt krav l eller 2, k ä n n e t e c k n a d av att en brikettpress (14) för det avskiljda materialet är an- ordnad efter den första sihemnßßh ochßakïemmdenfianfimfiasàüemfiCI2¥@>,Plant according to claim 1 or 2, characterized in that a briquette press (14) for the separated material is arranged after the first sihemnßßh ochßakïemmden fi an fi m fi asàüem fi CI2 ¥ @>, 4. Sätt för tillverkning av alkohol av pappersavfall innehål- lande papper, papp, kartong och/eller Wellpapp, laminerat eller kascherat med plast och/eller vax, karbonpapper, reklammaterial av olika slag och andra cellulosainnehållande material, k ä n - n e t e c k n a t av att pappersavfallet finfördelas, rensas och defibreras, att cellulosa i avfallet hydrolyseras till enk- lare sockerarter som förjäses och att den bildade alkoholen av-' destilleras.4. Methods of making alcohol from paper waste containing paper, cardboard, cardboard and / or corrugated cardboard, laminated or laminated with plastic and / or wax, carbon paper, advertising materials of various kinds and other cellulosic materials, characterized in that: the paper waste is pulverized, cleaned and defibrated, cellulose in the waste is hydrolyzed to simpler sugars which are fermented and the alcohol formed is distilled off. 5. Sätt enligt krav 4 eller 5, k ä n n e t e c k n a t av att fasta material avskiljes före hydrolysen och/eller efter jäsningen.5. A method according to claim 4 or 5, characterized in that solid materials are separated before the hydrolysis and / or after the fermentation. 6. Sätt enligt något av föregående krav, k ä n n e t e c k - n a t av att avskiljt, fast material pressas till briketter. 466 1566. A method according to any one of the preceding claims, characterized in that separated, solid material is pressed into briquettes. 466 156 7. Sätt enligt något av föregående krav, k ä n n e t e c k - n a t av att den avdestillerade alkoholen behandlas ytterliga- re för torkning och/eller avlägsnande av andra substanser.7. A method according to any one of the preceding claims, characterized in that the distilled alcohol is further treated for drying and / or removal of other substances.
SE8901311A 1989-04-12 1989-04-12 SETTING AND CONSTRUCTION FOR MANUFACTURING ENGINE SPRING OF CELLULOUS WASTE AND WASTE MATERIALS SE466156B (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
SE8901311A SE466156B (en) 1989-04-12 1989-04-12 SETTING AND CONSTRUCTION FOR MANUFACTURING ENGINE SPRING OF CELLULOUS WASTE AND WASTE MATERIALS
PCT/SE1990/000248 WO1990012103A1 (en) 1989-04-12 1990-04-11 Way and plant for producing alcohol for motor fuel from cellulose bearing waste and rest materials
AU54498/90A AU5449890A (en) 1989-04-12 1990-04-11 Way and plant for producing alcohol for motor fuel from cellulose bearing waste and rest materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE8901311A SE466156B (en) 1989-04-12 1989-04-12 SETTING AND CONSTRUCTION FOR MANUFACTURING ENGINE SPRING OF CELLULOUS WASTE AND WASTE MATERIALS

Publications (3)

Publication Number Publication Date
SE8901311D0 SE8901311D0 (en) 1989-04-12
SE8901311L SE8901311L (en) 1990-10-13
SE466156B true SE466156B (en) 1992-01-07

Family

ID=20375648

Family Applications (1)

Application Number Title Priority Date Filing Date
SE8901311A SE466156B (en) 1989-04-12 1989-04-12 SETTING AND CONSTRUCTION FOR MANUFACTURING ENGINE SPRING OF CELLULOUS WASTE AND WASTE MATERIALS

Country Status (3)

Country Link
AU (1) AU5449890A (en)
SE (1) SE466156B (en)
WO (1) WO1990012103A1 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19909328B4 (en) * 1998-11-06 2004-09-23 Christian Widmer Waste recovery operations
AU3789100A (en) * 1998-11-06 2000-05-29 Christian Widmer Method for utilizing waste
ES2303792B1 (en) 2007-02-15 2009-06-12 Industrias Mecanicas Alcudia S.A. A PROCEDURE FOR THE ENERGETIC REVALUATION OF THE ORGANIC FRACTION OF URBAN SOLID WASTE, AND INSTALLATION.
ES2373759T3 (en) * 2007-03-07 2012-02-08 Dsm Ip Assets B.V. PROCEDURE TO DRY AND PURIFY A MIXTURE OF CELLULOSE / PLASTIC RESIDUES IN PARTICLES.

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4425433A (en) * 1979-10-23 1984-01-10 Neves Alan M Alcohol manufacturing process

Also Published As

Publication number Publication date
WO1990012103A1 (en) 1990-10-18
SE8901311D0 (en) 1989-04-12
SE8901311L (en) 1990-10-13
AU5449890A (en) 1990-11-05

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