WO1995004153A1 - Procede et systeme de traitement biologique de dechets - Google Patents
Procede et systeme de traitement biologique de dechets Download PDFInfo
- Publication number
- WO1995004153A1 WO1995004153A1 PCT/NL1994/000166 NL9400166W WO9504153A1 WO 1995004153 A1 WO1995004153 A1 WO 1995004153A1 NL 9400166 W NL9400166 W NL 9400166W WO 9504153 A1 WO9504153 A1 WO 9504153A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- stream
- slurry
- waste
- high concentration
- fraction
- Prior art date
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims abstract description 17
- 239000004576 sand Substances 0.000 claims abstract description 27
- 239000002002 slurry Substances 0.000 claims abstract description 20
- 239000007787 solid Substances 0.000 claims abstract description 19
- 239000011368 organic material Substances 0.000 claims abstract description 17
- 239000000463 material Substances 0.000 claims abstract description 13
- 238000000855 fermentation Methods 0.000 claims abstract description 11
- 239000002245 particle Substances 0.000 claims abstract description 11
- 239000000470 constituent Substances 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract description 5
- 238000012216 screening Methods 0.000 claims abstract description 3
- 238000009434 installation Methods 0.000 claims description 15
- 238000009264 composting Methods 0.000 claims description 10
- 239000000126 substance Substances 0.000 claims description 7
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 6
- 238000000746 purification Methods 0.000 claims description 5
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims 1
- 238000000926 separation method Methods 0.000 description 7
- 239000004927 clay Substances 0.000 description 6
- 230000004151 fermentation Effects 0.000 description 6
- 239000010791 domestic waste Substances 0.000 description 5
- 239000011521 glass Substances 0.000 description 5
- 239000004575 stone Substances 0.000 description 5
- 239000002361 compost Substances 0.000 description 4
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- 230000007062 hydrolysis Effects 0.000 description 3
- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 239000010921 garden waste Substances 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 238000009996 mechanical pre-treatment Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 description 2
- 235000013311 vegetables Nutrition 0.000 description 2
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 239000004021 humic acid Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920000867 polyelectrolyte Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 210000004767 rumen Anatomy 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F9/00—Fertilisers from household or town refuse
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/40—Treatment of liquids or slurries
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/145—Feedstock the feedstock being materials of biological origin
-
- 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
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Definitions
- the invention relates to a method for the biological treatment of waste, comprising the processes of hydrolysing the waste, separating the hydrolysed material stream, by screening, into a relatively coarse organic fraction to be discharged and having particles larger than x, where x has a value between 1 and 5 mm. and a slurry stream having particles smaller than x, and converting dissolved organic components, by means of anaerobic fermentation, into biogas.
- a method for the biological treatment of waste comprising the processes of hydrolysing the waste, separating the hydrolysed material stream, by screening, into a relatively coarse organic fraction to be discharged and having particles larger than x, where x has a value between 1 and 5 mm. and a slurry stream having particles smaller than x, and converting dissolved organic components, by means of anaerobic fermentation, into biogas.
- the object of the invention is to overcome these drawbacks, to which end it is proposed, in the first instance, that the said slurry stream has the sand fraction between 2 and 1000 ⁇ separated therefrom and then, that the slurry stream which remains after removal of the sand fraction is separated into a stream having a high concentration of solid fine organic material and clay-like constituents and a water stream containing mainly dissolved organic components which are purified anaerobically in a bioreactor.
- the removal of sand preferably takes place in a hydrocyclone.
- the removed sand can be reprocessed to give a reusable quality.
- the waste remaining after removal of sand has been considerably reduced in weight. This leads to cost savings in the remaining processes.
- the wear on the equipment will likewise be considerably reduced.
- the step of separating into a stream having a high concentration of solid fine organic material and clay-like constituents and a stream, to be passed to the bioreactor end containing dissolved organic components is preferably carried out in a decanter centrifuge, providing the option of avoiding the use of chemicals, which is of great advantage for further processing.
- the stream obtained having a high concentration of solid fine organic material and clay-like constituents is subjected to dewatering and secondary composting. Another possibility is that of subjecting this stream to further treatment in a RUDAD reactor.
- the invention also relates to a system for the biological treatment of waste, comprising: a reactor for hydrolysing the waste, a screen installation for separating the hydrolysed material into a fraction larger than x, where x has a value between 1 and 5 mm, and a slurry containing a fraction smaller than x, and an anaerobic purification reactor for converting organic constituents dissolved in the slurry into biogas.
- the system is provided with a hydrocyclone for removing from the slurry the sand fraction between 2 and 1000 ⁇ and also with a decanter centrifuge for separating the slurry into a stream having a high concentration of solid fine organic material and a stream containing mainly dissolved organic components.
- the material having a high concentration of solid fine organic material which is produced by the decanter centrifuge, can be subjected to further treatment.
- Another possibility is the use of a RUDAD reactor for breaking down substances not readily degradable (especially cellulose fibres) .
- the invention will now be explained in more detail with reference to the flow sheet. A number of recirculation streams and bypass streams are not shown.
- admixture of air will suppress the formation of methane in the PRETHANE reactor, so that said formation of methane can take place subsequently in the UASB reactor under safe and controlled conditions.
- the temperature is maintained at 37 * 3°C, by means of a warm-water system.
- the pH is maintained between 5 and 6.5.
- the solids content between and 10%.
- the hydraulic retention time will be between 1 and 2 days.
- the retention time of the solids may vary between 2 and 5 days.
- the hydrolysed material is conveyed to the rotary screen 3 where it undergoes dewatering.
- the rotating rotary drum has a pore size between 1 and 5 mm, preferably between 2.5 and 3-5 mm.
- the fermenting mass from the PRETHANE reactor is separated, in the rotary drum, into a coarse organic fraction (coarse fibrous material) which may either be fermented further in the PRETHANE or RUDAD reactor or is dewatered mechanically and may then be subjected to secondary composting, and a slurry stream containing only small particles.
- This lastmentioned slurry stream containing small particles still contains fine sand, clay and organic material.
- dewatering takes place from 5-10% solids content in the incoming stream to ⁇ 13% in the stream of solid particles.
- This stream of solid particles can be further dewatered in the screw press 4, prior to the aerobic composting.
- the stream of solid particles can be dewatered to give ⁇ 55 of dry matter.
- Downstream of the screw press there may be, for example, a belt conveyor which passes the material to the aerobic composting installation.
- the liquid stream which still contains fine sand, clay and organic material is passed to the hydrocyclone 5 where the sand is separated. This separated sand is reprocessed in the installation 6. This reprocessed sand can be separated in a clean, reusable form.
- the slurry stream which flows from the hydrocyclone and from which the sand fraction has been removed, is pumped to the decanter centrifuge 7• This stream is separated therein into a water stream containing virtually only dissolved components which are conveyed to the anaerobic water purification installation 9. and a stream with a high concentration of fine organic material and clay ⁇ like substances which may be further processed in a system 8. This may consist of a PRETHANE or RUDAD fermentation reactor, a mechanical dewatering installation and/or a drying-composting installation.
- the stream containing dissolved components is processed to give pure water and biogas.
- the fermented residue contains such large amounts of contaminants (metals, organic microcontaminants, plastics) that it cannot and must not be used as a compost. It will therefore have to be dumped, or after incineration the residue has to be dumped.
- the sand can be separated in a clean form and thus need not be dumped.
- VFG Vegetable, Fruit and Garden waste 25,000 tonnes of VFG
Abstract
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU75092/94A AU7509294A (en) | 1993-07-30 | 1994-07-15 | Method and system for the biological treatment of waste |
DE4495582T DE4495582T1 (de) | 1993-07-30 | 1994-07-15 | Verfahren und Anlage zur biologischen Abfallaufbereitung |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL9301341A NL9301341A (nl) | 1993-07-30 | 1993-07-30 | Werkwijze en inrichting voor de biologische behandeling van afvalstoffen. |
NL9301341 | 1993-07-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1995004153A1 true WO1995004153A1 (fr) | 1995-02-09 |
Family
ID=19862719
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/NL1994/000166 WO1995004153A1 (fr) | 1993-07-30 | 1994-07-15 | Procede et systeme de traitement biologique de dechets |
Country Status (5)
Country | Link |
---|---|
AU (1) | AU7509294A (fr) |
DE (1) | DE4495582T1 (fr) |
MX (1) | MX9405799A (fr) |
NL (1) | NL9301341A (fr) |
WO (1) | WO1995004153A1 (fr) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0753495A2 (fr) * | 1995-07-11 | 1997-01-15 | Valorga Process | Procédé de production d'un amendement organique stabilisé, et installation pour la mise en oeuvre de ce procédé |
WO1997034851A1 (fr) * | 1996-03-15 | 1997-09-25 | Biophil Gmbh Gesellschaft Für Biotechnologie, Energie- Und Umwelttechnik Gmbh | Procede et installation de valorisation de dechets organiques et nouvelle installation de biogaz appropriee |
EP0866042A2 (fr) * | 1997-03-19 | 1998-09-23 | Lurgi Entsorgungstechnik GmbH | Procédé de traitement des déchets biologiques |
GB2329894A (en) * | 1997-10-01 | 1999-04-07 | Sobegina Trading Limited | Treatment of city's common waste to produce organic fertilisers |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19745896A1 (de) * | 1997-10-17 | 1999-04-22 | Babcock Anlagen Gmbh | Verfahren und Vorrichtung zur Aufbereitung von Abfall |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0142873A1 (fr) * | 1983-09-09 | 1985-05-29 | Gist-Brocades N.V. | Procédé et appareil pour la fermentation anaérobique de déchets solides en milieu aqueux en deux étapes |
DE3614865A1 (de) * | 1986-05-02 | 1987-11-05 | Kraemer Paul | Vorrichtung zur schlammaufbereitung |
EP0567184A1 (fr) * | 1992-04-24 | 1993-10-27 | N.V. Vuilafvoer Maatschappij Vam | Méthode de traitement des déchets de légumes, de fruits et d'autres produits de jardin |
-
1993
- 1993-07-30 NL NL9301341A patent/NL9301341A/nl not_active Application Discontinuation
-
1994
- 1994-07-15 AU AU75092/94A patent/AU7509294A/en not_active Abandoned
- 1994-07-15 DE DE4495582T patent/DE4495582T1/de not_active Withdrawn
- 1994-07-15 WO PCT/NL1994/000166 patent/WO1995004153A1/fr active Application Filing
- 1994-07-29 MX MX9405799A patent/MX9405799A/es unknown
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0142873A1 (fr) * | 1983-09-09 | 1985-05-29 | Gist-Brocades N.V. | Procédé et appareil pour la fermentation anaérobique de déchets solides en milieu aqueux en deux étapes |
DE3614865A1 (de) * | 1986-05-02 | 1987-11-05 | Kraemer Paul | Vorrichtung zur schlammaufbereitung |
EP0567184A1 (fr) * | 1992-04-24 | 1993-10-27 | N.V. Vuilafvoer Maatschappij Vam | Méthode de traitement des déchets de légumes, de fruits et d'autres produits de jardin |
Non-Patent Citations (1)
Title |
---|
DIETER SCHLAG ET AL.: "BETRIEBSANLAGEN ZUR VERGÄRUNG VON ABFÄLLEN", MÜLL UND ABFALL, vol. 25, no. 8, August 1993 (1993-08-01), BERLIN DE, pages 599 - 609 * |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0753495A2 (fr) * | 1995-07-11 | 1997-01-15 | Valorga Process | Procédé de production d'un amendement organique stabilisé, et installation pour la mise en oeuvre de ce procédé |
FR2736633A1 (fr) * | 1995-07-11 | 1997-01-17 | Valorga Process Sa | Procede de production d'un amendement organique stabilise de haute qualite, et installation pour la mise en oeuvre de ce procede |
EP0753495A3 (fr) * | 1995-07-11 | 1997-02-12 | Valorga Process Sa | |
WO1997034851A1 (fr) * | 1996-03-15 | 1997-09-25 | Biophil Gmbh Gesellschaft Für Biotechnologie, Energie- Und Umwelttechnik Gmbh | Procede et installation de valorisation de dechets organiques et nouvelle installation de biogaz appropriee |
EP0866042A2 (fr) * | 1997-03-19 | 1998-09-23 | Lurgi Entsorgungstechnik GmbH | Procédé de traitement des déchets biologiques |
EP0866042A3 (fr) * | 1997-03-19 | 1999-05-06 | Lurgi Entsorgungstechnik GmbH | Procédé de traitement des déchets biologiques |
GB2329894A (en) * | 1997-10-01 | 1999-04-07 | Sobegina Trading Limited | Treatment of city's common waste to produce organic fertilisers |
GB2329894B (en) * | 1997-10-01 | 2000-09-06 | Sobegina Trading Limited | A method for the treatment of city's common waste to produce organic fertilisers |
Also Published As
Publication number | Publication date |
---|---|
NL9301341A (nl) | 1995-02-16 |
DE4495582T1 (de) | 1996-08-22 |
AU7509294A (en) | 1995-02-28 |
MX9405799A (es) | 1995-01-31 |
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