WO2010084250A1 - Method and drying field for fuel peat production - Google Patents

Method and drying field for fuel peat production Download PDF

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Publication number
WO2010084250A1
WO2010084250A1 PCT/FI2010/050039 FI2010050039W WO2010084250A1 WO 2010084250 A1 WO2010084250 A1 WO 2010084250A1 FI 2010050039 W FI2010050039 W FI 2010050039W WO 2010084250 A1 WO2010084250 A1 WO 2010084250A1
Authority
WO
WIPO (PCT)
Prior art keywords
peat
drying
field
drying field
subsurface
Prior art date
Application number
PCT/FI2010/050039
Other languages
English (en)
French (fr)
Inventor
Kari Mutka
Timo NYRÖNEN
Original Assignee
Vapo Oy
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 Vapo Oy filed Critical Vapo Oy
Priority to EP10733279A priority Critical patent/EP2389425A1/en
Priority to RU2011134450/03A priority patent/RU2011134450A/ru
Publication of WO2010084250A1 publication Critical patent/WO2010084250A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10FDRYING OR WORKING-UP OF PEAT
    • C10F5/00Drying or de-watering peat
    • C10F5/02Drying or de-watering peat in the field; Auxiliary means therefor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/28Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B9/00Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
    • F26B9/10Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in the open air; in pans or tables in rooms; Drying stacks of loose material on floors which may be covered, e.g. by a roof

Definitions

  • the present invention relates to a method for producing fuel peat, in which - the peat is detached from the bog from the lifting area, the detached peat is transferred as a high-consistency mass, with a solids content of 8 - 30 %, preferably 15 - 25 %, from the bog to a drying field, which is a special base designed for drying, on which the transferred peat is spread as a thin layer and dried mainly by utilizing direct solar energy, in which case the peat dries through the effect of solar radiation and wind, and - after drying, the peat is transferred from the drying location to further use or storage.
  • the invention also relates to a drying field created to apply the method.
  • a so-called hydro-peat method for example GB 166,576, is known, in which a water jet is used to detach peat from a bog and pump it as a very thin sludge to a drying field, which is usually an area of bog taken out of production.
  • a drying field which is usually an area of bog taken out of production.
  • the mass is spread as a thin sludge and allowed to dry for several weeks, after which cuts, preferably as a briquette-sod pattern, are made at least in the longitudinal direction in the drying paste-like mat, when separate briquettes form as the mass dries.
  • cuts preferably as a briquette-sod pattern
  • Finnish patent FI-93855 discloses a peat-production method, in which wet peat is detached from a bog and collected in a stockpile at a selected place on the peat field, the dried side surface of which is turned at regular intervals to the other side. Even using this technique the production output remains modest .
  • EP 1524310 discloses a method according to the preamble, in which peat is transported some distance away from the production area to a special field to dry. Very good results in terms of production efficiency have been obtained using an asphalt field, but such a special field construction is very expensive. Conventional milled-peat pro- duction produces 500 MWh/ha. Using such a field method, and particularly using an asphalt field, drying outputs of 5000 - 10 000 MWh can be achieved. In terms of logistics, trailer transport is disadvantageous, in that the mass must be loaded a second time onto the spreading trailer. For this method, high-consistency-mass pumped transfer has been developed, though this too has the disadvantage of a second loading, unless complex automatic spreading machines are used.
  • the present invention is intended to create a simpler field method for peat production, the investment costs of which would be much lower than in the prior art, but which would otherwise exploit the advantages of the field method.
  • the invention is characterized by what is stated in the characterizing portion of Claim 1.
  • the characteristics of the drying field according to the invention are stated in Claim 11.
  • a bog surface can act as a drying base, if it is dried effectively and aged in order to alter its surface properties favourably.
  • Creating a drying field on a bog area requires efficient subsurface and perimeter drainage. At least the surface part of the bog must be compacted and dried, which typically takes 2 - 3 years, but at least one year.
  • the surface layer dries and hardens to a depth of a few centi- metres, while over time cell changes too take place.
  • the capillary properties of the field become favourable through drying.
  • the decomposed peat Once the decomposed peat has compacted and its surface has become very dry (typically to a 20 - 30-% moisture content) , it finally becomes water repellent and does not easily become wet. This does not happen on a normal production field, as the peat is harvested at a moisture content of about 40 % and a new fresh peat layer is always exposed once the previous layer has been milled off.
  • the surface layer becomes wet during heavy rain, but the slope of the field and the subsurface drains dry it rapidly. Under the thin dry surface layer, the moisture content is still quite high, typically 75 %, down to the subsurface- drainage depth. However, the fuel peat on top of it is dried to become considerably drier (e.g., 40-% moisture content) . In between is a thin dry surface layer, which rapidly dries if it becomes wet.
  • the field surface is not degraded, so that its structure remains good for drying material.
  • the few conditioning measures that may be necessary to maintain the profile of the field will create at most momentary drawbacks.
  • the method according to the invention can exploit short dry periods of a few days between periods of rain better than the prior art.
  • a second advantage is that the conditioned peat forms denser granules or sods than milled peat, which withstand rain and mechanical handling well.
  • the peat is spread on the drying field as small sods, i.e. lumps.
  • Spreading can be done using certain types of manure spreader.
  • the lumps are collected, when they disintegrate to form granular peat.
  • the advantage of granular peat is its greater gran- ule size compared to milled peat. Thanks to its larger granule size, granular peat's dust loss is considerably less than that of milled peat and it withstands rain better.
  • the properties of the fuel-peat product obtained correspond mainly to those of rough milled peat, but there are fewer fines in it and its thermal value and density are greater than those of milled peat .
  • sod-peat production the shape of the sod being spread is, as such, not decisive. However, it is preferable if the contact surface with the base is minimized, as with a corrugated sod.
  • Figure 1 shows the overall arrangement of the peat work site, as a layout diagram
  • Figure 2a shows a cross-section of a drying field with subsurface drainage
  • Figure 2b shows the moisture profile of a drying field without subsurface drainage
  • Figure 3 shows a top view of the drainage arrangement of the drying field of Figure 2.
  • the stages of the method are as follows :
  • the drying field is allowed to age and dry for at least one year, preferably for at least 2 - 3 years,
  • peat is detached from the bog in the lifting area, which is close (generally less than 1 km) from the drying field,
  • the peat is spread on the drying field to dry by a spreader device, so that the peat becomes lightly conditioned lumps
  • sod peat can be produced, in which more strongly conditioned peat is pressed through a nozzle to form sods that are substantially larger and denser than granules, which also have a compact surface. These remain in shape better than lumps when they are gathered into a ridge. Machines known from milled and sod-peat production can be used in ridging.
  • the drying field 12 is preferably located in the immediate vicinity of the lifting area 10 ( Figure 1) .
  • an excavator or other work machine can be used to lift the peat directly from the bog to the spreading trailer, which is used to transport the peat to the drying field 12 and spread it there.
  • a separate transfer can be used before loading the spreading trailer, if the distance is more than 500 m.
  • the drying field 12 is built on a field that has been taken out of production, on an old stockpile base, on new areas, preferably on a low edge area, in which there is a thin, 0, 3 - 1, 5-m, preferably 0, 5 - 1-m peat layer on top of the subsoil 14, according to Figure 2a.
  • a perimeter ditch is dug around an area of the selected size of the peat layer 16 and feeder ditches are dug at 20 - 40-m intervals.
  • the open ditches 18 extend down to the subsoil 14.
  • subsurface drains are laid in each strip, preferably in two layers, i.e. an upper layer at a depth of 0, 3 m (0,25 - 0, 5 m) and a lower layer at a depth of 0, 7 m (0, 4 - 0, 9 m) .
  • the upper subsurface-drain layer is about halfway down the peat layer 16, or slightly higher, while the lower layer is closer to the bottom of the ditch.
  • the perimeter and feeder ditches will be lower than the subsurface drains, so that water coming from the subsurface drains will flow into the feeder ditches and from there into the perimeter ditch.
  • the subsurface drains prevent the groundwater from rising by capillary action through the peat layer.
  • the subsurface drains are preferably pipe subsurface drains, because their operating life is not short. So-called mole drains can also be used.
  • Subsurface drains laid on two levels are advantageous, as the deep subsurface drains prevent water rising by capillary action and the subsurface drains on the surface dry the surface layer rapidly after rain. Thus, in all conditions, water is removed optimally. Without subsurface drainage, the groundwater level will extend nearly to the peat surface in the ridge between the feeder ditches, according to Figure 2b, when the moisture profile 22 of the ridge will typically be curved.
  • effective subsurface drainage refers to the ground- water level being reduced with the aid of subsurface drainage to a depth of at least 0,6 m, and also that the groundwater level will at no point rise close to the surface, but will remain everywhere at a considerably low level.
  • the subsurface drains are at intervals of 2,5 m (generally 2 - 10 m, preferably 2,5 - 5 m) . Every second subsurface drain is preferably deeper. Thus, subsurface drainage is preferably made to two levels 0,3 - 0,7 m apart from each other.
  • the subsurface drainage can also comprise transverse subsurface drains. If the subsurface drains are installed too widely apart in the peat layer, they will not be able to prevent sufficiently the water from rising by capillary action.
  • the width of a strip is generally 20 - 40 m. The length of a strip can be in the order of 100 m.
  • the drying field is sloping, so that most of the surface water can flow into the feeder ditches.
  • the fall of the drying field is 1:1000 - 5:100, preferably 1:100.
  • the fall can be made in the drying field, for example, with the aid of milling, before the field is aged.
  • the drying field is allowed to age for at least one year and preferably 2 - 3 years before starting production, when the thin surface of the peat layer 16, at a depth of a few centimetres, which is here marked as the layer 17', dries and its cellular structure disintegrates at least to some extent.
  • the surface of the peat layer then compacts and hardens and becomes a durable drying base, which allows water to percolate through it poorly.
  • the thin surface layer dries to become very dry and does not conduct water upwards by capillary action. Otherwise, the upper part 17 of the peat layer 16 dries to a moisture content of 75 % down to the subsurface drain level.
  • the limiting factor in lifting peat is the solids content of the raw peat, which should be more than 15 %.
  • the drier the raw peat the greater the drying result that will be achieved.
  • sod-peat production the maximum solids content of the raw peat is less than 20 %, as a spreading trailer cannot form a sod from peat as dry as that.
  • references to sod peat mean peat pieces, which have a granule size of more than 15 mm, with a small deviation.
  • milled-peat production there is no upper limit to the solids content, but a solids content of more than 30 % seldom appears.
  • a sufficiently dry layer on new bogs is generally 0,5 - 1,0 m and in old areas even as much as 2, 0 m (1, 5 - 2, 5 m) .
  • the peat lifted from the lifting area is transferred as a high- consistency mass with a solids content of 8 - 30 %, preferably
  • the peat is spread on the drying field as thin layers, preferably 2 - 5 cm (in other words, 16 - 40 kg/m 2 ) , which dry rapidly through the effect of sunlight and wind, in about 1 - 4 days, depending on the spreading thickness and the evaporation. Drying to the selected final moisture content takes place in a ridge, in which the peat is collected as granules or sods.
  • the dried fuel-peat product is transferred to a store, generally with a moisture content of at most 55 %, preferably 35 - 50 %.
  • the manure- spreader trailer divides the mass into small pieces and the mass is conditioned by being slightly compacted, so that lumps without fines arise.
  • the manure-spreader trailer includes a bottom conveyor (chain conveyor) as well as vertical screws, which throw the lumps onto the drying field, when the compacted lumps spread as somewhat flat sods on the surface of the drying field.
  • some other spreading device possessing a mechanically similar conditioning and spreading power.
  • the total number of the lumps at least 90 % are 20 - 200 g in weight and about 25 cm 2 (generally 15 - 100 cm 2 ) in size.
  • the drying of the lumps is facilitated by their size and shape, which give them a large surface area.
  • the lumps' contact surface area with the base is small, so that they also dry slightly from underneath.
  • One product obtained by using the method has properties that correspond to, or are somewhat better than rough milled peat.
  • the following values are used and achieved in spreading and production (the preferred target values appear in square brackets) :
  • the important factors used in the method are the aged and sloping peat surface of the drying field, which reduces the absorption of rainwater into the drying base. Thanks to the slope, most of the rainwater flows rapidly into the feeder ditches while, as a result of aging, the compacted surface does not absorb as much rainwater as a normal bog base.
  • the partly or already completely dried lumps can be collected in a ridge, when the lumps disintegrate into granules being, however, substantially coarser and denser than milled peat.
  • the granular peat is allowed to dry to the target dryness, after which it is transferred to further use or storage.
  • a granular-peat harvest can be gathered as many as 25 times in a season, i.e. the production cycle is rapid.
  • the granule size of the finished, dried fuel peat is 3 - 8 mm, preferably 4 - 6 mm, so that it is coarser that normal milled peat.
  • the surface of the drying field can be bound with a selected binder, particularly to reduce dust formation.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Treatment Of Sludge (AREA)
PCT/FI2010/050039 2009-01-23 2010-01-25 Method and drying field for fuel peat production WO2010084250A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP10733279A EP2389425A1 (en) 2009-01-23 2010-01-25 Method and drying field for fuel peat production
RU2011134450/03A RU2011134450A (ru) 2009-01-23 2010-01-25 Способ и сушильное устройство для производства топливного торфа

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20095056A FI20095056A0 (sv) 2009-01-23 2009-01-23 Förfarande för tillverkning av bränntorv
FI20095056 2009-01-23

Publications (1)

Publication Number Publication Date
WO2010084250A1 true WO2010084250A1 (en) 2010-07-29

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ID=40329513

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/FI2010/050039 WO2010084250A1 (en) 2009-01-23 2010-01-25 Method and drying field for fuel peat production

Country Status (4)

Country Link
EP (1) EP2389425A1 (sv)
FI (1) FI20095056A0 (sv)
RU (1) RU2011134450A (sv)
WO (1) WO2010084250A1 (sv)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2444471A2 (en) 2010-10-22 2012-04-25 Vapo Oy Method for producing peat
WO2014207295A1 (en) * 2013-06-24 2014-12-31 Biodiili Oy Method for producing peat
RU2690239C1 (ru) * 2018-10-31 2019-05-31 Федеральное государственное бюджетное учреждение "Всероссийский научно-исследовательский институт мелиорированных земель" (ФГБНУ ВНИИМЗ) Способ подготовки выработанного фрезерным способом торфяного месторождения для сельскохозяйственного использования
RU2783620C1 (ru) * 2021-12-21 2022-11-15 Николай Васильевич Сысоев Тепличный способ производства торфо-минеральных удобрений и топлива

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI791313A (fi) * 1978-04-24 1979-10-25 Einar Karlsson Foerfarande foer torvhantering
SU1314071A1 (ru) * 1985-04-16 1987-05-30 Всесоюзный научно-исследовательский институт торфяной промышленности Способ добычи торфа
EP1524310A1 (en) * 2003-10-17 2005-04-20 Vapo Oy Method and equipment for producing horticultural and fuel peat and a fuel peat product

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI791313A (fi) * 1978-04-24 1979-10-25 Einar Karlsson Foerfarande foer torvhantering
SU1314071A1 (ru) * 1985-04-16 1987-05-30 Всесоюзный научно-исследовательский институт торфяной промышленности Способ добычи торфа
EP1524310A1 (en) * 2003-10-17 2005-04-20 Vapo Oy Method and equipment for producing horticultural and fuel peat and a fuel peat product

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2444471A2 (en) 2010-10-22 2012-04-25 Vapo Oy Method for producing peat
EP2444471A3 (en) * 2010-10-22 2014-05-07 Vapo Oy Method for producing peat
WO2014207295A1 (en) * 2013-06-24 2014-12-31 Biodiili Oy Method for producing peat
RU2690239C1 (ru) * 2018-10-31 2019-05-31 Федеральное государственное бюджетное учреждение "Всероссийский научно-исследовательский институт мелиорированных земель" (ФГБНУ ВНИИМЗ) Способ подготовки выработанного фрезерным способом торфяного месторождения для сельскохозяйственного использования
RU2783620C1 (ru) * 2021-12-21 2022-11-15 Николай Васильевич Сысоев Тепличный способ производства торфо-минеральных удобрений и топлива

Also Published As

Publication number Publication date
EP2389425A1 (en) 2011-11-30
RU2011134450A (ru) 2013-02-27
FI20095056A0 (sv) 2009-01-23

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