• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    In a method for at least two-stage drying of garbage, in particular household waste, in which the waste is pre-dried in a first stage and finally dried in a second stage, wherein the drying comprises an aerobic decomposition, in which the biodegradable organic fractions of the waste under supply are degraded microbially of air and heat generation, is deposited in a first portion of a closed building moist refuse the first drying stage and in a second portion of the closed building heaped pre-shredded waste is subjected to the second drying stage, wherein the second drying stage, the aerating the pre-dried waste by introducing, in particular, blowing in air from outside the building and the first drying step comprises ventilating the moist waste by sucking the air coming from the second drying step through the moist M spilled out of the building.
    公开号:AT518659A4
    申请号:T393/2016
    申请日:2016-08-24
    公开日:2017-12-15
    发明作者:
    申请人:Holcim Technology Ltd；
    IPC主号:
    专利说明:

    The invention relates to a process for at least two-stage drying of waste, in particular household waste, in which the waste is predried in a first stage and finally dried in a second stage, wherein the drying comprises an aerobic decomposition, in which the organically easily decomposable organic fractions of the waste be microbially degraded with the supply of air and heat.
    The invention further relates to a device for carrying out such a drying process.
    There is a desire to have alternative fuels, i. For example, to make fuels with a reduced calorific value compared to high-grade natural gas, coal or petroleum useful, for example, in the cement clinker production process, such alternative fuels often being available in the form of refuse. Garbage is available in large quantities as household waste. Household waste means a waste mixture originating from private households and similar institutions. With regard to the relevant waste separation regulations, household waste is often referred to as household residual waste. The material composition of household waste varies regionally and seasonally. Household waste usually contains varying amounts of plastic, fine waste, paper / cardboard, diapers, textiles, glass, metal, composite material and vegetables. From a fuel technology point of view, household waste can be subdivided into the components water, inert substance, fossil fuel substance and organic fuel substance, it also being noted that household waste contains a high proportion of organic substances, ie. approx. 30-60% (organic fraction incl. water).
    Previously, the utilization potential for such wastes in the cement industry was limited due to the significant moisture content, when the waste materials are introduced directly into the burner systems, which has led to increased heat demand in the clinker production process for evaporation of the water due to the water content. In addition, resulting from the significant amount of water introduced after the evaporation of the water unfavorably high volume of total process exhaust gases, which in turn leads to increased effort in the exhaust management.
    In order to be able to use domestic waste in the cement industry as an alternative fuel, a pretreatment including drying is required accordingly. Typically, the drying is carried out using high quality expensive fuels, such as natural gas or diesel, but this is disadvantageous in economic terms. Alternatively, the waste may be subjected to biological drying.
    Under biological drying is generally understood a process in which household waste is aerated and thus flows through air and rotting aerobically. The household waste is hereby introduced into a reactor and the supply of oxygen, the biodegradable organic components of household waste are mined microbially. The decomposition of the organic components by microorganisms is an exothermic reaction, which causes an increase in temperature within the waste. In this case, however, only a small part of the organic components of the waste is decomposed, whereby the
    Energy is largely retained and the household waste remains usable as a high-energy substitute fuel. The biological heat produced during aerobic rotting causes the household waste to dry. By means of the energy released in this process, the air flowing through the household waste absorbs heat and moisture and thereby causes a reduction in the moisture content within the household waste. After biological drying, household waste can be used as a high-quality, C02-neutral substitute fuel in the cement production process.
    The biological drying requires as an external source of energy only power for driving the ventilation system and is thus far more energy efficient and cheaper than the above-mentioned, fossil fuels requiring drying methods.
    In contrast to other composting processes, biological drying aims to make household waste useable as a high-quality substitute fuel with the shortest possible residence time in the reactor. Firstly, the energy content in household waste is increased by the greatest possible removal of the water and secondly, a large part of the calorific value of the organic matter within the refuse obtained, since only a minimal, organic degradation takes place.
    The biological drying can be carried out in one or two or more stages. In the context of the present invention, a two-stage or multi-stage process is proposed in which the moist waste of a
    Predrying and the pre-dried waste is subjected to a final drying.
    A disadvantage of the two-stage drying is that two rotting chambers or compartments, each with its own ventilation system and its own exhaust air treatment system are required, so that the equipment cost is significantly increased. Furthermore, the heat loss in two Rottekammern compared to single-stage drying is greater.
    It is therefore an object of the invention to provide a method and a device with which the aforementioned disadvantages can be overcome without great device complexity.
    To solve this problem, the invention provides in a method of the type mentioned that in a first sub-area of a closed building dumped moist waste is subjected to the first drying stage and in a second portion of the closed building heaped pre-dried waste the second drying stage is subjected, wherein the second drying step comprises aerating the pre-dried waste by introducing, in particular, blowing in air from outside the building and the first drying step comprises aerating the wet waste by sucking the air coming from the second drying step through the wet waste out of the building.
    The invention thus provides, on the one hand, that the at least two drying stages are carried out in the same building, with no separate, closed ones
    Rotting chambers or the like. Are required, but the garbage in a first or second portion of the building is simply heaped up to at least a pile or at least a rent. The expenditure on equipment is thereby considerably reduced. If the first and the second subarea of the building are arranged adjacent to one another or in a common space, the transport of pre-dried waste from the first subarea to the second subarea is facilitated. The transport of pre-dried waste from the first portion to the second portion preferably comprises picking up the pre-dried waste (e.g., with an excavator bucket), transporting it, and dumping it in the second portion. Due to the fact that after the first drying stage, the moist waste is heaped up as predried waste in the second part of the closed building, recycling, homogenization and loosening of the waste is achieved, which favors the drying process.
    In particular, this breaks open dead zones and settlements, which would adversely affect the permeability of the air. Overall, this reduces the drying time, the drying dimensions and the energy consumption.
    The first and the second subarea of the building each occupy a partial area of the base of the building and are preferably arranged on the same level. This facilitates the transport of pre-dried waste for final drying.
    On the other hand, the invention provides that the same air is used for the aeration of the refuse in the first and in the second drying step. The air is here in the
    Run countercurrently to the drying progress through the two drying stages, i. first used for final drying and then for pre-drying. Fresh air from outside the building is thus first passed through the already pre-dried waste, in particular pressed to perform the final drying, whereby the air is heated and humidified. The heated air is then used for the ventilation of the wet waste in the first part of the building and then sucked out of the building. Because preheated air is already used for predrying, the drying process can be carried out with the same or lower energy consumption in a shorter time. The transfer of the coming out of the predrying air for final drying takes place with respect to the arrangement of the two drying stages in the same building, especially in a common space or volume of the building in a simple manner that from the second drying step passing through the garbage exiting air the humid waste is sucked out of the building.
    The inventive method requires only a single exhaust air treatment system, so that the equipment cost is reduced compared to conventional methods.
    Furthermore, blowers and lines for the second drying stage must not necessarily be made corrosion resistant, because fresh air is not corrosive in contrast to the exhaust air.
    A preferred embodiment provides that the introduction, in particular blowing in of the air in the pre-dried waste via a perforated or slotted, the pre-dried waste bearing soil takes place. The holes or slots may in this case have a conically downwardly enlarging cross-sectional area in order to prevent clogging. The suction of the air is preferably carried out through the wet garbage through a perforated or slotted, the wet garbage carrying soil. The ventilation system thus requires only a perforated or slotted bottom with underlying plenum (false floor) in the second part of the building with a fan, in particular pressure fan to direct ambient air through the pre-dried waste, and a perforated or slotted floor in the first part of the building with a Suction fan to pull the air through the wet garbage and blow it outwards.
    The first and second portions of the building are preferably in open communication with each other, so that no separate lines are required for transporting the air coming out of the final drying for pre-drying.
    Alternatively, however, the first and the second subarea of the building can also be connected to each other by an air duct. This is particularly advantageous in the case where the air used for the ventilation is subjected to dehumidification or condensation after passing through the second drying stage.
    Another preferred method provides that fresh air is sucked in via a fresh air flap of the building. The sucked-in air flow is preferably adjustable, so that the amount of fresh air introduced in the time unit can be regulated as a function of measured values. The fresh air is used together with the air coming from the second drying stage for aeration of the wet waste in the first drying stage. By adjusting the amount of fresh air, the mixing ratio of fresh air to preheated air from the second drying stage can be adjusted. The admixture of fresh air can be used, for example, to reduce the moisture content of the air coming from the second drying stage. The control of the sucked fresh air is preferably carried out by the fact that more air is sucked out of the building through the perforated or slotted bottom of the first drying stage as is blown through the bottom of the second drying stage.
    A parallel, continuous operation of the first and the second drying stage is preferably made possible by the fact that the first portion of the building is divided into a plurality of sections, which are successively filled with moist waste, so that the sections are filled in the process with waste of different degrees of drying , The individual sections of the first subarea can preferably be filled one after the other with moist waste at a time interval of one day. Also, the second portion of the building is preferably divided into a plurality of sections, which are successively filled with pre-dried waste from the first drying stage, so that the sections are filled during operation with waste of different degrees of dryness. The individual sections of the second subarea can preferably be filled with moist refuse one after the other at a time interval of one day. This makes it possible to successively coat the pre-dried waste from the respective highest degree of pre-drying or the longest length of time into the final drying stage.
    In the final drying stage, it is possible to proceed analogously, with a preferred process management in this connection providing that the section of the second drying stage having the highest degree of drying is emptied and the removed, end-dried waste is removed.
    Furthermore, it is preferably provided that the highest degree of dryness portion of the first drying stage is emptied, the removed, pre-dried waste is poured into an empty section of the second drying stage and new moist waste is poured up in the emptied section. This achieves a successive replenishment of new, moist waste. The subdivision of the first and / or second subarea of the building into sections thus allows a replenishment of new, wet garbage and a redeployment of pre-dried garbage for final drying, without interrupting the drying process with respect to the sections not affected by reloading got to.
    If the sections, as corresponds to a preferred embodiment, are elongate and adjoin one another with their longitudinal sides, in particular in a row, the recharge or the
    Shifting the garbage of each section from the narrow side of the sections made, so easy access while ensuring space-saving arrangement is guaranteed. The space-saving arrangement here means that the sections with their long sides directly, possibly with the interposition of limiting elements, such as. Boundary walls, between the sections, adjoin one another. The waste can be poured in the individual sections up to a height of 3m, preferably up to a height of 4m, so that large amounts of waste can be dried.
    In an energetically preferred manner it can be provided that the first drying step is carried out over a longer period of time than the second drying step. Accordingly, it can preferably be provided that the first subarea of the building has a higher number of sections than the second subarea of the building. This ensures a procedure in which the garbage in the individual sections of the predrying step and the final drying step is allowed to linger for approximately the same length and no section of the preliminary or final drying step remains empty. If the sections e.g. are filled one after the other at a distance of one day, and after filling all sections of each having the highest degree of dryness portion is emptied, whereupon it is filled with new garbage, results in a training with 10 sections a residence time of the garbage in each section of 10 days.
    With regard to the dwell time, it is preferably provided that the moist waste collected in a section over a period of 8-12, in particular 10 days of the first
    Is subjected to drying step. The pre-dried waste collected in one section can preferably be subjected to the second drying step over a period of 4-8, in particular 5 days.
    An advantageous division of the drying progress between the predrying and the final drying stage is achieved in a preferred process by the fact that the wet waste in the first drying stage to reduce the water content to 25-35% dried and the pre-dried waste in the second drying stage to the reduction of Water content is dried to 15-2SI.
    The extracted from the building air is preferably subjected to air purification, in particular one using a bio-filter. Because the air according to the invention has passed through both drying stages, it is ensured that the latter has a sufficient moisture content which allows safe operation of the biofilter, in particular drying out of the filter being avoided. Furthermore, with regard to the high moisture content of the air extracted from the building, the pre-connection of a wet scrubber in front of the filter can be dispensed with.
    According to a further aspect of the invention, there is provided an apparatus for carrying out the drying method according to the invention comprising a building with a perforated or slotted bottom in a first part of the building and a perforated or slotted floor in a second part of the building, with the perforated or slotted one Bottom of the second portion associated blower, in particular pressure blower for introducing, in particular blowing air from the environment of the building over the perforated or slotted bottom disposed on the floor waste and standing with the perforated or slotted bottom of the first portion suction fan for sucking air from waste placed on the floor over the perforated or slotted floor into the environment of the building.
    The suction fan is preferably connected to an air purification device arranged outside the building.
    The invention will be explained in more detail with reference to an embodiment schematically illustrated in the drawing.
    In Fig. 1 is a flow diagram of a waste processing according to the invention including a drying including the intended for drying building is shown. To be processed moist or wet waste 1, if necessary, after a check for radioactivity, a crushing device 2 is supplied, in which the waste is crushed to a size of example meadow <200 mm. The shredded waste is subjected at 3 to a magnetic separation of metallic components, wherein the metallic components 4 are separated out. The crushed moist waste is brought to the building 5 for drying and dried in two stages. In a first partial area 6 of the building, a predrying takes place and in a second partial area 7 of the building, a final drying takes place. In the first and in the second partial area 6, 7, a perforated floor 8 or 9 is respectively provided, via which the supply and removal of drying air takes place. The supply of ambient air 10 takes place with the aid of a plurality of pressure blowers 11, which suck in ambient air 10 from outside the building 5 and blow through the perforated bottom 9 in the 9 thrown up on the floor pre-dried waste 12 The ventilation can be designed so that one Both can blow and suck, but usually the air is blown. As a result, the pre-dried waste 12 is aerated and the air emerging from the refuse 12 passes, as indicated at 13, from the second subarea 7 of the building 5 into the first subarea 6. In the first subarea 6, the air is released by the action of the plurality of suction fans 14 pulled through the wet refuse 15 and passes as moist air 16 through the perforated floor 8 from the building 5 addition. The moist air 16 is freed of suspended matter 18 in a biofilter 17.
    The dried garbage 19 is removed from the building 5 and subjected to further use, e.g. supplied as fuel for cement production.
    The seepage water 20 accumulating in the chambers of the perforated bottom 8 and 9 is likewise removed and can be supplied to a work-up 21.
    The first portion 6 and the second portion 7 are each divided into a plurality of sections 22. The sections 22 need not be structurally separated. The perforated bottom 8 or 9 has a plurality of chambers 23, wherein each section 22 is assigned its own chamber 23, so that the ventilation in each section 22 can be adjusted individually.
    权利要求:
    Claims (18)
    [1]
    claims:
    1. A process for at least two-stage drying of garbage, in particular household waste, in which the waste is predried in a first stage and finally dried in a second stage, wherein the drying comprises an aerobic decomposition, wherein the biologically decomposable organic fractions of the garbage under supply microbially degraded by air and with evolution of heat, characterized in that in a first sub-area of a closed building dumped moist waste is subjected to the first drying stage and in a second portion of the closed building heaped pre-dried waste the second drying step is subjected, the second drying step the Aerating the pre-dried waste by introducing, in particular, blowing in air from outside the building, and the first drying step comprises aerating the wet waste by sucking the air coming from the second drying stage t through the damp garbage out of the building.
    [2]
    2. The method according to claim 1, characterized in that the introduction of the air in the pre-dried waste via a perforated or slotted, the pre-dried waste carrying soil takes place.
    [3]
    3. The method according to claim 1 or 2, characterized in that the suction of the air through the moist waste through a perforated or slotted, the wet waste carrying soil takes place.
    [4]
    4. The method of claim 1, 2 or 3, characterized in that the first and the second portion of the building are in open connection with each other.
    [5]
    5. The method according to any one of claims 1 to 4, characterized in that the wet waste after the first drying step is piled up as pre-dried waste in the second part of the closed building.
    [6]
    6. The method according to any one of claims 1 to 5, characterized in that the first portion of the building is divided into a plurality of sections, which are successively filled with moist waste, so that the sections are filled during operation with garbage different degrees of dryness.
    [7]
    7. The method according to any one of claims 1 to 6, characterized in that the second portion of the building is divided into a plurality of sections, which are successively filled with pre-dried waste from the first drying stage, so that the sections in the current process with garbage different degrees of dryness are filled. 8. Method according to claim 7, characterized in that the section of the second drying stage having the highest degree of dryness is emptied and the removed, end-dried waste is removed.
    [9]
    9. The method according to any one of claims 6 to 8, characterized in that the highest degree of dryness having portion of the first drying stage is emptied, the removed, pre-dried waste is poured up in an empty section of the second drying stage and heaped up new wet waste in the emptied section becomes.
    [10]
    10. The method according to any one of claims 6 to 9, characterized in that the sections are elongated and adjoin one another with their longitudinal sides, in particular arranged in a row.
    [11]
    11. The method according to any one of claims 1 to 10, characterized in that the first drying step is carried out over a longer period than the second drying step.
    [12]
    12. The method according to any one of claims 6 to 11, characterized in that the first portion of the building has a higher number of sections than the second portion of the building.
    [13]
    13. The method according to any one of claims 6 to 12, characterized in that the recorded in a section of moist waste over a period of 8-12, in particular 10 days of the first drying step is subjected.
    [14]
    14. The method according to any one of claims 7 to 13, characterized in that the wetted in a section pre-dried waste over a period of 4-8, in particular 5 days of the second drying stage is subjected.
    [15]
    15. The method according to any one of claims 1 to 14, characterized in that the wet waste is dried in the first drying step to reduce the water content to 25-35%.
    [16]
    16. The method according to any one of claims 1 to 15, characterized in that the pre-dried waste is dried in the second drying step to reduce the water content to 15-25%.
    [17]
    17. The method according to any one of claims 1 to 16, characterized in that the extracted from the building air is subjected to air purification, in particular using a bio-filter.
    [18]
    18. An apparatus for carrying out a method according to any one of claims 1 to 17, comprising a building with a perforated or slotted bottom in a first portion of the building and a perforated or slotted bottom in a second portion of the building, one with the perforated or slotted bottom the second sub-area associated fan, in particular pressure fan for introducing, in particular blowing air from the environment of the building over the perforated or slotted bottom disposed on the ground waste and standing with the perforated or slotted bottom of the first portion suction fan to Drawing in air from waste placed on the floor over the perforated or slotted floor into the environment of the building.
    [19]
    19. The apparatus according to claim 18, characterized in that the suction fan is in communication with an air purification device arranged outside the building.
    类似技术:
    公开号 | 公开日 | 专利标题
    DE3024813C2|1988-05-26|
    EP0809777B1|2001-02-14|Process and device for drying organic waste
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    DE3725988C2|1995-11-16|Process for humidifying sewage sludge
    EP3289299A1|2018-03-07|Method for treating waste
    DE4019389C2|1992-04-16|
    EP0458738B1|1996-06-19|Process for composting sewage sludge contaminated with harmful substances together with waste wood by aerobic fermentation and use of the product so obtained
    EP1051372B1|2002-05-02|Method and device for drying organic waste
    EP1226883A1|2002-07-31|Method for separating a mixture of residual waste
    DE3531605A1|1987-05-21|Reactor for the treatment of organic materials and process for obtaining several intermediate and final products from these materials
    DE2100636A1|1972-07-20|Composting organic waste - partic household garbage
    EP0508383A1|1992-10-14|Control and measurement method for the biological drying of sewape sludge
    DE2810911C2|1986-03-20|Process for composting waste materials
    DE4312923A1|1994-10-20|Process for the treatment of waste products made from vegetable substances and products made from vegetable substances, in particular food waste, that are reusable as bio-valuable substances
    DE3736889A1|1988-06-01|Method for preparing organic wastes by composting
    DE2721349B2|1981-03-19|Process for composting sewage sludge or other organic waste in an aerobic continuous operation
    DE19846336A1|1999-09-23|Treating refuse containing both inert and organic materials
    DE19734319A1|1999-02-11|Process conditioning wet residues by drying, composting and loosening-up
    EP0691316B1|1999-07-28|Process and device for aerobic decaying of organic substances
    EP0810983B1|2000-04-19|Process and device for composting organic substances
    EP1180499A2|2002-02-20|Process for transforming into humus an aqueous suspension of organic matter, especially sewage sludge
    DE102019001500A1|2020-09-10|Process for treating residues from fermentation and apparatus for fermenting biogenic waste
    EP1408021A2|2004-04-14|Process and apparatus for biological drying of residual waste, sewage sludge and/or biomass
    DE2423891A1|1975-12-04|Adsorptive carbon production method - uses slag produced by refuse coking or degasification process
    DE10125408A1|2002-05-02|Treatment of municipal waste comprises removing recyclable materials, mechanically grinding and sieving remaining material and mixing medium with part of fermenter, product being fermented to produce biogas used to generate electricity
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE2937390A1|1979-09-15|1981-03-19|Nemetz, Herbert, 6369 Schöneck|Mfg. compost by decomposing organic waste in mechanised silo - which conveyor and compacts with min. wear of moving parts|
    EP0541184A1|1991-11-08|1993-05-12|Veluwse Afval Recycling B.V.|Process and device for composting organic material|
    DE19804949A1|1998-02-07|1999-08-12|Lurgi Entsorgungstechnik Gmbh|Method and device for drying organic waste|
    EP0623572B1|1993-05-07|1997-01-29|Bühler Ag|Digestion shed with flexible guiding and conditioning of airflows|
    DE19739864A1|1997-09-11|1999-03-18|Dornier Gmbh Lindauer|Process for treating the exhaust air from thermal drying processes, in particular from processes during the drying of sewage sludge in sewage sludge dryers and plant for carrying out the process|CN111623602B|2020-05-06|2021-09-24|大连理工大学|Novel rotary biological drying device|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA393/2016A|AT518659B1|2016-08-24|2016-08-24|Method and device for drying garbage|ATA393/2016A| AT518659B1|2016-08-24|2016-08-24|Method and device for drying garbage|
    MA046040A| MA46040A|2016-08-24|2017-08-17|METHOD AND DEVICE FOR DRYING WASTE|
    RS20210558A| RS61815B1|2016-08-24|2017-08-17|Method and device for drying of waste|
    MX2019001632A| MX2019001632A|2016-08-24|2017-08-17|Method and device for drying of waste.|
    CA3034772A| CA3034772A1|2016-08-24|2017-08-17|Method and device for drying of waste|
    PCT/IB2017/000980| WO2018037273A1|2016-08-24|2017-08-17|Method and device for drying of waste|
    EP17761565.5A| EP3504495B8|2016-08-24|2017-08-17|Method and device for drying of waste|
    ES17761565T| ES2879701T3|2016-08-24|2017-08-17|Procedure and device for drying residues|
    CR20190068A| CR20190068A|2016-08-24|2017-08-17|Method and device for drying of waste|
    ARP170102327A| AR109390A1|2016-08-24|2017-08-23|METHOD AND DEVICE FOR WASTE DRYING|
    PH12019500373A| PH12019500373A1|2016-08-24|2019-02-21|Method and device for drying of waste|
    HRP20210687TT| HRP20210687T1|2016-08-24|2021-05-03|Method and device for drying of waste|
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