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WO2006039770A1 - Equipment and system destined for drying solid organic matter and utilization of the resulting product - Google Patents

Equipment and system destined for drying solid organic matter and utilization of the resulting product Download PDF

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Publication number
WO2006039770A1
WO2006039770A1 PCT/BR2005/000215 BR2005000215W WO2006039770A1 WO 2006039770 A1 WO2006039770 A1 WO 2006039770A1 BR 2005000215 W BR2005000215 W BR 2005000215W WO 2006039770 A1 WO2006039770 A1 WO 2006039770A1
Authority
WO
WIPO (PCT)
Prior art keywords
chamber
waste
resulting product
utilization
organic matter
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.)
Ceased
Application number
PCT/BR2005/000215
Other languages
French (fr)
Inventor
Jorge Cortizo Carvalho
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.)
MUNDO LIMPO SA
Original Assignee
MUNDO LIMPO SA
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 MUNDO LIMPO SA filed Critical MUNDO LIMPO SA
Publication of WO2006039770A1 publication Critical patent/WO2006039770A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B11/00Machines or apparatus for drying solid materials or objects with movement which is non-progressive
    • F26B11/02Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles
    • F26B11/028Arrangements for the supply or exhaust of gaseous drying medium for direct heat transfer, e.g. perforated tubes, annular passages, burner arrangements, dust separation, combined direct and indirect heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B1/00Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids
    • F26B1/005Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids by means of disintegrating, e.g. crushing, shredding, milling the materials to be dried
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B11/00Machines or apparatus for drying solid materials or objects with movement which is non-progressive
    • F26B11/02Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles
    • F26B11/04Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis
    • F26B11/0436Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis comprising multiple stages, e.g. multiple rotating drums subsequently receiving the material to be dried; Provisions for heat recuperation

Definitions

  • This invention application is for a household solid waste (HSW) transformation system, which dehydrates and reduces waste volume through grinding and heat shock-induced moisture extraction, while controlling gas emissions in the points of suppression and combustion tolerance and sending such gases into a cyclone, from where they are sent to a gas treatment unit.
  • the process seeks the utilization and the waste final destination, with control of the emission of gas particles from the treatment system to the atmosphere, thereby preventing the generation of leachate, the proliferation of vectors, the use of land fills and waste dumps, and especially the contamination of groundwater and the creation of holes in the ozone layer, as it impedes the generation of methane and carbon gases, which are produced by the decomposition of organic waste.
  • This invention is the result of nearly ten (10) years of research on the subject by the inventor, who has other previously applied patents pending, until the gravimetric, physical and chemical properties of household solid wastes were fully understood, making possible the development of a system capable to efficiently dehydrating and reducing waste volume, with the possibility of reusing the resulting product in various applications.
  • the main components of this dehydration system are a first dryer assembly comprising one or more dryers connected in parallel, with lower working temperature, and a second dryer assembly, connected in series in relation to the first dryer assembly, which second assembly is identical in all aspects to the first drier assembly except for its higher working temperature, which is controlled by outer panels.
  • the product obtained with this system may be used as a source of energy for the process itself. It may also be pressed into billets to replace firewood in furnaces or power plants. Yet another application is the use of the product for waterproofing the ground before paving, or in the manufacturing of bricks, blocks, etc. for civil construction.
  • the rotary ⁇ ier in question is entirely novel and has great use to the public. It is designed to treat household solid waste (HSW), through waste volume reduction and dehydration, while controlling particle emission and treating the gases produced.
  • HSW household solid waste
  • FIGURE 1 illustration of the of the stages and operation of the drier for the process in question;
  • the unit has a feed inlet (2) for the waste coming from the grinder (1), which waste descends a guide ramp (3) installed on the upper inner part of a gas furnace (4), which will heat the air to be used to feed the drying system.
  • the drying system comprises a drier mounted on two support bases (5), coupled to a motor (6), with a central treatment chamber (7) that is kept at a temperature ranging from 60° C to 100 ° C, in the first stage of treatment.
  • the heat produced in the gas furnace (4) circulates through the treatment chamber (7), driven by a powerful suction blower (8), raising the temperature inside the main body to dehydrate the waste, which is then guided by fins (9) installed along the entire length of the treatment chamber (7), from where the material (13) exits for final disposal. Due to the heat shock, which causes dehydration, the organic waste releases gases and particles, which due to their properties and with the assistance of the suction blower are guided through a duct to the gas and particles treatment unit (10).
  • Each dryer chamber is supported by two concrete bases (5).
  • a motor (6) is installed to the first of these bases to drive a gear (11), which in turn drives the treatment chambers.
  • gear (11) which in turn drives the treatment chambers.
  • gear (11) There is also a guide wheel (12) on each support base (5) to enable rotation of the assemblage.
  • the solid matter is sent to a second grinder (1') through a waste reception nozzle inlet (2'), conducted along a guide ramp (3'), which is also installed on the upper inner part of a gas furnace
  • the elements of the second dryer will be the same as the elements of the first dryer, except temperature, which will range from 200° C to 250 ° C in the second stage of treatment.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Treatment Of Sludge (AREA)
  • Drying Of Solid Materials (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

Equipment and system destined for drying solid organic matter and utilization of the resulting product, characterized by the fact that the dehydration chamber has feed inlet (2) to receive the waste that comes from a grinder (1), descending a ramp (3) installed on the upper part of a gas furnace (4). The waste is conducted to the central treatment chamber (7), which is supported on two supporting bases (5), the first of which also sustains a motor (6) that drives a gear (11), which in turn drives the dryer (7). Both bases have a pair of guide wheels (12). The Heat produced by the furnace (4) circulates inside the chamber (7), driven by the suction of a powerful outer blower (8), thereby increasing the temperature and pressure inside the chamber to treat the material, which is guided by fins (9) through the chamber and dehydrated while the particles and gases produced by the system are guided by a duct to the treatment unit.

Description

"EQUIPMENT AND SYSTEM DESTINED FOR DRYING SOLID ORGANIC MATTER AND UTILIZATION OF THE RESULTING PRODUCT"
This invention application is for a household solid waste (HSW) transformation system, which dehydrates and reduces waste volume through grinding and heat shock-induced moisture extraction, while controlling gas emissions in the points of suppression and combustion tolerance and sending such gases into a cyclone, from where they are sent to a gas treatment unit. The process seeks the utilization and the waste final destination, with control of the emission of gas particles from the treatment system to the atmosphere, thereby preventing the generation of leachate, the proliferation of vectors, the use of land fills and waste dumps, and especially the contamination of groundwater and the creation of holes in the ozone layer, as it impedes the generation of methane and carbon gases, which are produced by the decomposition of organic waste.
This invention is the result of nearly ten (10) years of research on the subject by the inventor, who has other previously applied patents pending, until the gravimetric, physical and chemical properties of household solid wastes were fully understood, making possible the development of a system capable to efficiently dehydrating and reducing waste volume, with the possibility of reusing the resulting product in various applications.
The use of this system is only possible thanks to the equipment developed especially for this purpose, which is basically made up of a rotary drier with unique features, that is, it enables organic compounds do be dehydrated, without igniting, until they are completely dry, while at the same time it impedes particles and gases produced in the system from being released into the atmosphere or the environment.
The main components of this dehydration system are a first dryer assembly comprising one or more dryers connected in parallel, with lower working temperature, and a second dryer assembly, connected in series in relation to the first dryer assembly, which second assembly is identical in all aspects to the first drier assembly except for its higher working temperature, which is controlled by outer panels.
As the invention in question is a modular system, it can be arranged otherwise, depending on specific requirements, and further units with the same characteristics may be coupled to form a single unit with the same capability to generate a contaminant-free dehydrated product.
The product obtained with this system may be used as a source of energy for the process itself. It may also be pressed into billets to replace firewood in furnaces or power plants. Yet another application is the use of the product for waterproofing the ground before paving, or in the manufacturing of bricks, blocks, etc. for civil construction.
The rotary φier in question is entirely novel and has great use to the public. It is designed to treat household solid waste (HSW), through waste volume reduction and dehydration, while controlling particle emission and treating the gases produced.
The invention is entirely comprehensible in the flowchart that accompanies and supports this documentation and by the description below, which contains the same reference numbers included to the attached drawing and describes the arrangement and operation of the rotary drier, enabling one to easily comprehend the entire arrangement, its parts and components: FIGURE 1 - illustration of the of the stages and operation of the drier for the process in question;
As seen in Figure 1, the unit has a feed inlet (2) for the waste coming from the grinder (1), which waste descends a guide ramp (3) installed on the upper inner part of a gas furnace (4), which will heat the air to be used to feed the drying system. The drying system comprises a drier mounted on two support bases (5), coupled to a motor (6), with a central treatment chamber (7) that is kept at a temperature ranging from 60° C to 100 ° C, in the first stage of treatment. The heat produced in the gas furnace (4) circulates through the treatment chamber (7), driven by a powerful suction blower (8), raising the temperature inside the main body to dehydrate the waste, which is then guided by fins (9) installed along the entire length of the treatment chamber (7), from where the material (13) exits for final disposal. Due to the heat shock, which causes dehydration, the organic waste releases gases and particles, which due to their properties and with the assistance of the suction blower are guided through a duct to the gas and particles treatment unit (10).
Each dryer chamber is supported by two concrete bases (5). A motor (6) is installed to the first of these bases to drive a gear (11), which in turn drives the treatment chambers. There is also a guide wheel (12) on each support base (5) to enable rotation of the assemblage.
Subsequently, the solid matter is sent to a second grinder (1') through a waste reception nozzle inlet (2'), conducted along a guide ramp (3'), which is also installed on the upper inner part of a gas furnace
(4'), which furnace will heat the air that feeds the second drying system
(7'). The elements of the second dryer will be the same as the elements of the first dryer, except temperature, which will range from 200° C to 250 ° C in the second stage of treatment.
Through this process, after being pre-dried, grinded twice, and treated in at least two rotary drying chambers fed by heat from a gas furnace and thermal shock, with temperature ranging from 60° C to 100° C in the first stage and 200° C to 250° C in the second stage, the organic matter is entirely dehydrated and its volume is reduced to 20% of the original volume, resulting in a product that can be used in civil construction in the form of bricks and as a replacement for firewood used in furnaces, after being pressed.

Claims

1 - EQUIPMENT AND SYSTEM DESTINED FOR DRYING SOLID ORGANIC MATTER AND UTILIZATION OF THE RESULTING PRODUCT, characterized by the fact that it is a modular dehydration unit comprising a feed inlet (2) for the waste coming from the grinder (1), which waste descends a guide ramp (3) that is installed on the upper part of a gas furnace (4). The waste is conducted to the central treatment chamber (7), which is supported by two bases (5), the first of which also supports a motor (6), which drives a gear (11), which in turn drives the dryer (7). On both bases there is a pair of guide wheels (12). The heat produced by the furnace (4) circulates inside the chamber (7), driven by a powerful outer blower (8), thereby increasing the temperature and pressure inside the chamber to treat the material, which is guided by fins (9) through the chamber and dehydrated as the particles and gases produced by the system are guided by a duct to a treatment unit.
2 - EQUIPMENT AND SYSTEM DESTINED FOR DRYING SOLID ORGANIC MATTER AND UTILIZATION OF THE RESULTING PRODUCT, according to claim 1, is characterized by the fact that it comprises at least two drying chambers (7-7'), connected in series, with the same components, and preceded by grinders (1-1'). The temperature of the first drying chamber (7) ranges from 6O0C and 1000C and that of the second chamber (7') ranges from 2000C to 2500C, and the thermal shock dehydrates the material.
3 - RESULTING PRODUCT, obtained according to the claims above, characterized by the fact that the dehydrated organic material may be used as source of energy for the process itself; or pressed into billets to replace firewood in furnaces; or used in the manufacturing of bricks, or other elements for civil construction.
PCT/BR2005/000215 2004-10-15 2005-08-14 Equipment and system destined for drying solid organic matter and utilization of the resulting product Ceased WO2006039770A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
BRPI0404514-9A BRPI0404514A (en) 2004-10-15 2004-10-15 equipment and system for drying solid organic matter and use of the resulting product
BRPI0404514-9 2004-10-15

Publications (1)

Publication Number Publication Date
WO2006039770A1 true WO2006039770A1 (en) 2006-04-20

Family

ID=36147982

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/BR2005/000215 Ceased WO2006039770A1 (en) 2004-10-15 2005-08-14 Equipment and system destined for drying solid organic matter and utilization of the resulting product

Country Status (2)

Country Link
BR (1) BRPI0404514A (en)
WO (1) WO2006039770A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2437016A3 (en) * 2010-10-01 2017-11-01 ALBA 2 Energy GmbH Method for drying domestic waste and drying drum for same

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2323289A (en) * 1941-04-07 1943-07-06 Monolith Portland Cement Compa Coal drier
US3585730A (en) * 1969-01-17 1971-06-22 George W Morse Method and apparatus for the preservation of nutrients in forage
US5337496A (en) * 1986-10-29 1994-08-16 Enviro-Gro Technologies Sludge treatment process

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2323289A (en) * 1941-04-07 1943-07-06 Monolith Portland Cement Compa Coal drier
US3585730A (en) * 1969-01-17 1971-06-22 George W Morse Method and apparatus for the preservation of nutrients in forage
US5337496A (en) * 1986-10-29 1994-08-16 Enviro-Gro Technologies Sludge treatment process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2437016A3 (en) * 2010-10-01 2017-11-01 ALBA 2 Energy GmbH Method for drying domestic waste and drying drum for same

Also Published As

Publication number Publication date
BRPI0404514A (en) 2006-06-06

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