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 MATERIALSInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/02—Preparation of oxygen-containing organic compounds containing a hydroxy group
- C12P7/04—Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
- C12P7/06—Ethanol, i.e. non-beverage
- C12P7/08—Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate
- C12P7/10—Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate substrate containing cellulosic material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION 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
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics 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)
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)
| 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)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4425433A (en) * | 1979-10-23 | 1984-01-10 | Neves Alan M | Alcohol manufacturing process |
-
1989
- 1989-04-12 SE SE8901311A patent/SE466156B/en not_active IP Right Cessation
-
1990
- 1990-04-11 AU AU54498/90A patent/AU5449890A/en not_active Abandoned
- 1990-04-11 WO PCT/SE1990/000248 patent/WO1990012103A1/en not_active Ceased
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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