EP3965965A1 - Procédé hydrothermique et installation de traitement de déchets solides - Google Patents

Procédé hydrothermique et installation de traitement de déchets solides

Info

Publication number
EP3965965A1
EP3965965A1 EP20722214.2A EP20722214A EP3965965A1 EP 3965965 A1 EP3965965 A1 EP 3965965A1 EP 20722214 A EP20722214 A EP 20722214A EP 3965965 A1 EP3965965 A1 EP 3965965A1
Authority
EP
European Patent Office
Prior art keywords
waste
process according
plant
ofmsw
hydrothermal treatment
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
EP20722214.2A
Other languages
German (de)
English (en)
Inventor
Nazareno GIORGI
Lucio SANASI
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tpa Srl
Original Assignee
Tpa Srl
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 Tpa Srl filed Critical Tpa Srl
Publication of EP3965965A1 publication Critical patent/EP3965965A1/fr
Pending legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • B09B3/45—Steam treatment, e.g. supercritical water gasification or oxidation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • 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

Definitions

  • the present invention relates to a process for treating OFMSW (Organic Fraction of Municipal Solid Waste).
  • OFMSW Organic Fraction of Municipal Solid Waste
  • the invention relates to a process capable of improving the recycling efficiency of OFMSW, with the aim of developing a circular and sustainable economy.
  • the present invention relates to a process for the hydrothermal treatment of OFMSW for producing material suitable for biogas production by means of anaerobic digestion, with reduced production of solid digestate and greatly reduced odorous impact.
  • the present invention also concerns a plant for carrying out the process of the present invention.
  • OFMSW denotes the organic fraction of municipal solid waste resulting from the differentiated waste collection. Disposal of OFMSW is a highly felt socio-environmental problem. Interest in OFMSW as a source of biofuels for sustainable development originates from both the need of managing increasing amounts of such a differentiated waste, and the need of replacing crops preferably intended for animal nourishment, such as cereals, hay, maize silage, in feeding plants for biogas production.
  • OFMSW coming from the collection by means of skips may contain very different materials, such as metals, plastics, glass, inorganic inert materials such as gravel, and non bio -degradable materials such as bones, fruit stones, nut shells, crustacean shells and mollusc shells.
  • OFMSW essentially contains substances of organic nature, with a high availability of carbon-to-carbon chemical bonds that makes OFMSW potentially suitable for biological processes of valorisation and recovery, such as fermentation, in order to obtain biogas, as well as a stabilised solid residue that can be used in agriculture as soil amender or fertiliser.
  • OFMSW is treated in aerobic composting plants for compost production or in anaerobic digestion plants with biogas production. Said plants originate some serious practical problems as far as valorisation and recovery are concerned, which problems are caused by the lack of qualitative uniformity and the poor structuring capability of the waste to be treated.
  • the organic fraction of OFMSW has a high fermentability that facilitates arising of putrefactive phenomena with strong odorous emissions, which phenomena are accentuated by the prolonged permanence of great masses of material undergoing fermentation.
  • the prior art plants treating OFMSW generate environmental impacts of various kinds resulting from the release and the natural percolation, particularly evident in summer months, of the drainage liquid fraction originating from the organic matter, the leachate.
  • the leachate produced due to its intrinsic characteristics, is a source of unpleasant smells and of high processing and/or disposal costs.
  • the conventional composting and bio-gasification plants occupy very wide surfaces and are scarcely compact.
  • the prior art also teaches mechanically or hydraulically separating the organic fraction from the non-digestible fraction including metals, plastics, glass, inorganic inert materials and non-biodegradable material, in order to increase the biological potential of OFMSW.
  • the presence of metals, plastics, glass, inorganic inert materials and non- digestible materials in the mass to be treated can cause serious drawbacks and damages to the selecting and sorting machines. More particularly, a disadvantage consists in pump and pipe abrasion, as well as in the clogging of reservoirs.
  • WO 2006/048008 A2 concerns a method for decomposing biologic material, in which the material is conveyed to a tank in order to make it percolate by means of sieving. The leachate thus obtained is subsequently introduced again in order to modulate biogas production and thus to obtain more electric power in periods in which such power is more valuable, typically in order to meet peaks of electric power demand during the day.
  • the present invention provides a process for the hydrothermal treatment of OFMSW for the production of a pasty material that can be handled, is uniform, has reduced volume and weight, is sanitised and sterilised and has low odorous impact, which material can advantageously be used, upon a treatment for eliminating inorganic inert materials and non-digestible substances, in order to feed third- party plants for the production of biogas.
  • Another aspect of the process of the present invention is heat recovery performed by steam tapped from the hydrothermal treatment of OFMSW. Moreover, being such steam rich in micronized nutrients, it can advantageously be fed, after heat recovery, to a fast biodigester plant for the production of power necessary to the economy of the process of the present invention.
  • a further aspect of the process of the present invention is the collection and forwarding of the leachate, obtained from the unloading and the handling of OFMSW, to the fast biodigester plant mentioned above, thereby avoiding the prolonged permanence of the leachate with consequent arising of putrefactive phenomena and odorous emissions.
  • Yet another aspect of the process of the present invention concerns the transformation time of the arriving OFMSW, including a cycle of 8 - 10 hours, advantageously shorter than the permanence time of OFMSW, typically 20 - 30 days per cycle, as is the case for instance in the conventional anaerobic digestion plants.
  • the present invention concerns a plant for carrying out the process of the present invention, the diagram of which will be illustrated by the description below.
  • OFMSW refers to the putrescible organic material with high humidity content coming from the differentiated collection of municipal waste and consisting of food residues or waste. Collection usually takes place at domestic users or at selected users (such as canteens, restaurants, food industries and so on) according to management models referable to the use of specific street containers or to the collection at the premises of the concerned users (regulatory references: Decree of the Regional Council of 15 June 2006, No. 76, and Decree of the Regional Government of 25 February 2005, No. 568).
  • fast biodigester plant refers to an equipment of the plant of the present invention intended for the production in situ, according to techniques known per se, of biogas necessary to the economy of the process of the present invention.
  • carbon-to-carbon chemical bonds refers to an intrinsic characteristic of the organic matter in OFMSW and such bonds are a feeding source for methanogenic bacteria responsible for the production of biogas in anaerobic digestion.
  • SC Separatation Chamber
  • the term "SC (Separation Chamber) device” refers to the equipment where the hydrothermal treatment of OFMSW in the process of the present invention takes place.
  • the SC device is an equipment derived from Patent of Invention IT-0001416920 and Patent for Utility Model IT-0000280277.
  • the process according to the invention allows building a complete hydrothermal and mechanical industrial plant, with very low environmental impact, for the fast treatment of putrescible organic substances, even in admixture with various solids, such as inert materials, plastics, metals etc.
  • the plant according to the invention is capable of treating such a material according to a continuous process, without creating accumulations, even in great amounts and by producing materials directly utilisable as clean organic matter, clean metals, inert materials and plastics.
  • the process of the present invention includes a first aspect in which material 1, in loose condition or contained in bags, after having been weighted, is discharged on the ground in the suitable receiving yard 2 for the compulsory visual inspection.
  • the leachate is collected and sent, with the aid of suitable pumps, to pre-tank 5 feeding fast biodigester plant 6.
  • the leachate can optionally be submitted to a physical treatment, such as filtering through a fine mesh grid 4, in order to retain solid particles 7.
  • the latter can optionally be sent to dosing system 8.
  • Receiving yard 2 and dosing system 8 when provided, are preferably confined within a suitable restricted space with reduced size, preferably a size slightly exceeding the size necessary for containing waste and for allowing loading and unloading operations. That space is kept under a small negative pressure to prevent bad smells from diffusing to the outside.
  • the reduced size advantageously allows a rapid, cheap and effective depuration of the odorous atmosphere existing inside said space.
  • the restricted space can be obtained by means of a structure made of plasterboard or the like, having an opening for the material introduction, which can be closed.
  • Digestate 9 leaving fast biodigester plant 6 is divided into solid digestate 10 and liquid digestate 11.
  • a fraction 12 of the liquid digestate, after the depuration treatment in 13 by means of techniques known per se, provides water that can be sent to accumulation tank 14 and used for the needs of the plant of the present invention for treating OFMSW.
  • part of the water depurated in 13 is sent, after thermal exchange in exchanger 15, to boiler 16 for production of pressurised hot water 19 to be used for the hydrothermal treatment in SC devices in 17.
  • a fraction 13a of the depurated water is used for washing OFMSW receiving yard 2 at the end of the daily shift in order to eliminate residues of organic material and leachate.
  • the resulting liquid is recycled to pre-tank 5 feeding fast biodigester plant 6.
  • Biogas 35 produced in fast biodigester plant 6 is used as combustible gas for feeding boiler 16 intended for producing pressurised hot water 19 necessary for the OFMSW hydrothermal treatment in 17.
  • the material from receiving yard 2 is loaded onto a dosing system 8 which loads it onto a conveyor belt in order it can be forwarded to SC devices in 17 in a predetermined amount each said SC device is capable of receiving.
  • SC devices in 17 in a predetermined amount each said SC device is capable of receiving.
  • the material coming from dosing system 8 is submitted to a hydrothermal treatment with pressurised water 19 in the SC devices in 17, at suitable temperatures and for suitable times.
  • Hydrothermal treatment with pressurised water 19 in the SC devices combined with the hydraulic and mechanical shearing forces acting in said devices, besides separating inert fractions from the organic matter, produces a pasty material that can be handled, is uniform, has reduced volume and weight, is sanitised and sterilised and has a high potential of carbon-to-carbon chemical bonds and a low odorous impact. That material can be advantageously used, upon a treatment for eliminating inorganic inert materials and non-digestible substances, in order to feed third-party plants for the production of biogas through anaerobic digestion
  • the methanogenic potential of the material treated according to the hydrothermal process of the present invention has proven to be significantly higher than the methanogenic potential of the same, unprocessed material. Due to its characteristics, such a material can replace food crops for the production of biogas, either alone or co-digested with other matrices, such as sewage and dejects coming from farms for intensive animal breeding.
  • hydrothermal treatment of OFMSW with pressurised hot water 19 produces saturated steam that can be extracted and condensed in exchanger 15, thereby providing a liquid rich in nutrients such as carbohydrates, proteins, alcohols, fats, organic acids and other micronized organic substances, which can be advantageously used for feeding fast biodigester plant 6.
  • Laboratory tests have shown that such a liquid is excellent in terms of yield and quality of the anaerobic fermentation: the net production of biogas takes place in few days, preferably in about five days.
  • treatment of OFMSW in the SC devices in 17 includes the following steps:
  • pressurised hot water in which pressurised hot water 19, preferably at 250°C and about 40 bars, coming from boiler 16, is introduced into the SC device;
  • hydrothermal treatment in which the mass is treated at a temperature preferably in the range 150°C to 170°C for about 30 minutes; under such conditions, also sterilisation and stabilisation of the treated material, which no longer can undergo putrefactive phenomena, are achieved;
  • venting in which pressure is restored down to atmospheric pressure and temperature is lowered, preferably below 100°C, thereby enabling the subsequent safe opening of the SC device; the saturated steam extracted, rich in micronized nutrients; yields heat in exchanger 15 and, after condensation, it is sent to pre-tank 5 feeding fast biodigester plant 6;
  • loading takes place automatically, through the following steps:
  • six SC devices are sequentially fed in the period of about 1 hour elapsing between the loading and the unloading of the first SC device in 17.
  • the loading and the unloading of the SC devices take place by keeping the blades in a slight rotation in order to assist in spreading and handling the mass.
  • unloading of the SC chambers can be facilitated by means of a small jet of recovery water coming from accumulation tank 14.
  • the predetermined OFMSW amount, in weight, transferred to each SC device is one ton
  • the SC device only needs recycled water, coming from water treatment in 13.
  • the water is then pre-heated in exchanger 15 and converted into pressurised hot water by means of boiler 16.
  • the material unloaded from the SC devices is sent, by means of a conveying and lamination plate, to a conveyor belt that carries it to solid-liquid separator 20, through which the material being processed is divided into a liquid-pasty flow 21 and a solid flow 22.
  • liquid-pasty flow 21, comprising mixed organic materials and fine inert materials, is divided by means of a settler 23 into fine solid inert materials 26, e.g. glass, destined for a subsequent collection, and organic pasty material 24, having a high methanogenic potential thanks to the hydrothermal treatment it has been submitted to, which is collected by means of pumping, e.g. by means of a lobe pump, and sent, by means of tank trucks 25, to third-party plants for the production of biogas. Excess water 34 from settler device 23 is sent to pre-tank 5 and hence destined for fast biodigester plant 6.
  • solid flow 22 containing non-biodegradable material, metals, plastics and inorganic inert materials, is collected in 27 and divided into its merchandising components by means of techniques known per se.
  • Solid flow 22 is transferred to a conveyor belt, and ferrous and non-ferrous metals are recovered by means of ferrous metal separator 28 and non-ferrous metal separator 29 and sent to collection skips 30 and 31 for being recycled.
  • Remaining material 29a essentially including inorganic inert materials and plastics, is sent to waste material containers 32 and hence to collection 33.
  • a heterogeneous organic material has been prepared by mixing 2.5 kg of bread, 2.5 kg of vegetables, 2.5 kg of fruit waste and 2.5 kg of cooked pasta.
  • the matrix produced in this manner has been suitably divided into portions of 2 kg each, packaged in ultra-light and compostable bags.
  • the bags have been kept at 28 - 30°C and 60 - 80% relative humidity (values that are typically attained in summer season) and then used for the tests in the subsequent 48 hours,
  • the plant for carrying out the process of the present invention in accordance with the preferred embodiment thereof has a capacity of about 30,000 tons/year of OFMSW treated, corresponding to 100 tons/day, sufficient to serve a urban conglomeration of about 250,000 inhabitants, considering a per capita OFMSW production of about 110 Kg/year per inhabitant.
  • the plant occupies about 7,000 square metres, i.e. about one fifth of a prior art composting plant.

Landscapes

  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Processing Of Solid Wastes (AREA)
  • Catalysts (AREA)
  • Working-Up Tar And Pitch (AREA)

Abstract

L'invention concerne un procédé de traitement des fractions organiques des déchets solides municipaux (OFMSW), comprenant une étape initiale dans laquelle le lixiviat résultant de l'évacuation et de la manipulation de l'OFMSW est collecté et envoyé à une installation de biodigesteur rapide. L'OFMSW est ensuite soumis à un traitement hydrothermique au moyen d'eau chaude sous pression. Le matériau pâteux organique résultant des opérations de traitement et de division du matériau sortant du traitement hydrothermal de l'OFMSW est collecté et envoyé à des installations tierces pour la production de biogaz. L'invention concerne également une installation pour la mise en œuvre du procédé de la présente invention.
EP20722214.2A 2019-05-06 2020-05-06 Procédé hydrothermique et installation de traitement de déchets solides Pending EP3965965A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT102019000006578A IT201900006578A1 (it) 2019-05-06 2019-05-06 Processo di trattamento idro-termico della FORSU e impianto per la realizzazione di detto processo
PCT/IB2020/054290 WO2020225748A1 (fr) 2019-05-06 2020-05-06 Procédé hydrothermique et installation de traitement de déchets solides

Publications (1)

Publication Number Publication Date
EP3965965A1 true EP3965965A1 (fr) 2022-03-16

Family

ID=67551618

Family Applications (1)

Application Number Title Priority Date Filing Date
EP20722214.2A Pending EP3965965A1 (fr) 2019-05-06 2020-05-06 Procédé hydrothermique et installation de traitement de déchets solides

Country Status (3)

Country Link
EP (1) EP3965965A1 (fr)
IT (1) IT201900006578A1 (fr)
WO (1) WO2020225748A1 (fr)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114160544A (zh) * 2021-12-03 2022-03-11 深圳市英策科技有限公司 用于处理固体废物的方法及设备

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004053615B3 (de) * 2004-11-03 2006-05-18 Brandenburgische Technische Universität Cottbus Abbauverfahren von biogenem Material
ITTO20130914A1 (it) * 2013-11-12 2014-02-11 Lucio Sanasi Idrolizzatore termico per sostanza organica agente a temperatura, pressione ed agitazione con la combinazione dello sminuzzamento del materiale organico, tale da renderlo pronto alla biodigestione rapida. il raggiungimento della temperatura viene ott

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Publication number Publication date
IT201900006578A1 (it) 2020-11-06
WO2020225748A1 (fr) 2020-11-12

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