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Патент USA US2406509

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Aug- 27,1946;
CLAES-WILHELM PAL-.0
2,406,509 '
METHOD OF AND’ APPARATUS FOR'CARBONIZING PEAT
_ Filed Feb. 11, 1944
PREDR YING
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AFTEE
DRYING
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CARBON’
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Patented Aug. 27, 1946
' 2,406,509
UNITED STATES PATENT OFFICE‘
RJIETHOD OF AND APPARATUS FOR
CARBONIZIN G 'PEAT
Claés-Wilhelm Pilo, rstockholm, Sweden
Application February 1944, Serial No.'521,95’2
In Sweden December 22, 1942
11 Claims. (01.202-16)
2,
' The present invention relates to a method for
’ of the 'hot' peat coal and simultaneously obtain
continuous drying of material in solid form and
for partly or completely carbonizing peat;or
such a reduction of the temperature of the peat
coal as to decrease the riskof self-ignition when .
other solid carbonaceous material which con
sists substantially of carbon compounds and
water.
'
the peat coal contacts the'air, a gas vapor mix
_ ture which, Withoutpassing thegsuperheater, is
p
‘ led off by means of the fan [9 from the gas vapor
The invention is described below, reference
mixture withdrawn, from the after-drying zone,
being had to the accompanying drawing, which
is admitted into the shaft below the carbonizing
shows a plant according to the invention par
ticularly intended for part carbonization of peat. 10. '_ Thelower-most shaft portion 2 is formed as
. In the plant according to the drawing, peat
cooling chamber ‘and may be separatedv from
the moisture contents of which are about 50 %' for
the'upper zonesby means of a shutter I4. 0001-,
zone.
example, is charged into the top of a vertical
shaft. _The peat sinks through the shaft, pass- '
7
‘
;
U
_
I
ing air is sucked by a fan ,H from an inlet open-' »
ing l2 through the material in the cooling cham
ber and, then‘, discharged into the. preheater 2'9
ing va predrying zoneiin which the moisture con
tents are reduced to about 30 to 35%, then an
belonging to. _the__conld.ensingv apparatus and
after-drying zone in which the rest of the mois
through the ‘fanfamfrom where, possibly after
ture leaves, and ?nally a carbonizing zone, in
mixing with ?ue gases from the superheatenit
which the hemicellulose is disintegrated.
isadmitted into the uppermost. portion of the
The required heat is supplied by a superheater 20 shaft; thus part of the natural heat of the peat
5 connected to a furnace which may be heated
coal can be recovered, and at the‘ same time a
with peat. This superheater heats a vapor quan
fan can be spared,
tity circulating through the carbonizing Zone ‘and
Theready carbonized peat is subjected to me-. 7
the after-drying zone, the‘ said vapor being held
chanical compression at a point in the lower
in circulation by a fan £9, The vapor is self 25 portion of the shaft. After having been com
formed at the start of theplant, the airbeing
expelled. During the drying continued genera
pressed, the. material is allowed to fall down
into the lowermost portion of the shaft, which '.
tion of vapor takes place, excess of vapor being
portion is formed as ajho’oling chamber and
led off to a condensing battery 8 in which'the
otherwise held separatedirfrom the rest of the
vapor through condensation gives off heatto an 30 shaft by a movable shut'éo?" member. ~InYthe;
air quantity ?owing to the predrying zone, the
plant according to the drawing there are ar-.
said air being blown forth by a fan 9.
.
According to the embodiment‘of the invention,
illustrated on the drawing, some vapor circula
tion is also provided for through the after-dry
ing zone only. The object of this vapor circu
lation is to increase the heat transfer to the peat
by increased vapor speed and to reduce the tem
ranged in the shaft a number of'pivoted screens
I3, which‘ at the bottom may be. provided with
oblique surfaces as shownv in the drawing, the
35 said screens being ‘adapted to be actuated from
the outside by hand ‘wheels. and to be locked in
different positions. When the screens
swung inwards, the material between the
‘ perature in the lower portion of the after-dry
“screens” is compressed.‘ Thereafter the shut
ing zone in such a way that no carbonization 40 ter l4 closing the cooling chamber 2 is displaced
takes placein the said after-drying zone because
it would then be more dif?cult to remove the
moisture remaining in the center of the peat
column.
‘
All the circulating gas quantities may be
varied, for instance by controlling the speed of
the fans.
‘
To the hot air by which the predrying is ef
fected in the uppermost portion of the shaft,
toward one side of the shaft by the actuation of
a toothed wheel 15 engaging a toothed reckon
the lower side ‘of the shutter, so that the com
pressed material falls down into the cooling
chamber which is then closed by the shutter M '
being returned to its closing position. The
screens l3 are then'turned back to their initial
positions permitting the material to sink down
on to the shutter. After the carbonized peat has
flue gases from the superheater 5 are admitted 50 been cooled, it is removed through the discharge
in the plant according to the drawing, the said
?ue gases, together with fresh air which has
absorbed heat from the condenser 8, being
opening 4. The grate and the dscharge open
ing are preferably arranged in such a way that
the carbonized product can be easily discharged‘
pressed into the shaft by the fan 9.
direct into a wagon or to some other conveying
In order to recover part of the natural heat 55 device.
2,406,509 ,
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3>
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into and led off from the shaft through openings
extending around the shaft, the said opening be
ing connected to annular chambers l6 surround‘
ing the shaft casing, the said, chamber having
tangential inlet and outlet conduits, respectively.
As shown, the annular chambers l?qmay- com
municate with the shaft‘through a plurality ‘of
openings I‘! directed obliquely downwards; this
r
recirculating the superheated part of the stream
into the bottom, of the carbonizing zone, with
drawing a second gas stream from the after-dry:
ing zone, and utilizing said second gas stream to
' heat the gas current to be passed through the pre»
is of particular advantage in the upper portion,
_,
4
the column of peat at the top of the after-dryin
zone, recirculating one part of saidjgas stream
directly into the bottom of the after-drying zone,
recirculating a second part of said gas stream
directly into said shaft below said carbonizing
zone, superheating a third part of said gas stream,
‘Preferably, the gas and vapor are admitted
of the shaft where a low gas speed is, desired. _
'Vdrying zone.
. In order torsuck the vapor from the interiorof
the shaft, a suction pipe l8 extends from the ~
‘
'
Q ~ 5. In a method as claimed in claim 1, the steps
of superheating the gas current to be passed
center of the shaft, the opening of’ the said pipe
through the carbonizing zone by means of, a
being covered with a net when comminuted ma 15 v‘furnace and introducing the flue gases from said
terial is treated._
‘
1
7' i V,’ _‘_;
" furnace’into the gas current to be passed through
The invention has nowwith reference to the
the predrying zone.
accompanying drawing been describedas relat- ,
6. In a method as claimed, in claim 1, the step
ing to part-carbonization of peat. However,
of cooling the carbonized peat at the bottom of
the shaft by passing ‘a gaseousimedium through
. fundamentally thev same method may beused
withfadvantage for complete carbonization! of
'peat as well as for drying of other material,
whereby the drying, if desired, may be,_ followed
byv aheat treatment for other purposes, as for‘
' example for complete carbonization.
the column of material at the bottom of the shaft,
withdrawing saidgaseous medium from the shaft ;
and introducing it into a gas current to be passed
25
Having now describedrmy invention, whatlI
claim as new and desire to secure by Letters'Pat
ent is:
1. A, continuous method of converting peat ‘into
a solidrfueLrwhich method comprises feeding-the
raw‘ peat to be converted from above into a Y‘
‘ shaft: and permitting‘ it to sink continuously, in
a coherent column 'of substantially uniformv
cross-section, through three successive zones of ;
said shaft while passing throughithe uppermost I
predrying zone of the. shaft in‘countercurrent to
the descending peat a hot gas current consisting
to at ieasta considerable part of hot air, passing
'
through the predrying zone;
7
'
=
.
'
‘
'7. Apparatus for drying peat, comprising a ver- 7
. ticalshaft including a predrying zone at its top,
' an after-drying zone below said predrying zone,’
and ~ a . carbonizing , zone-below said ‘after-drying
30'
zone, an inletinto said predryingrzone ‘nearer to' V
the-bottom than. to the top of the latter, an air
conduit having one end connected'to said inlet
and its other end open to the atmosphere, a fan
inserted into saidair'conduit to force air through
said conduit into and'through said predrying
zone‘ in countercurrent to the descending mate
rial, a vapor discharge conduit near the top of
said after-drying zone, a vapor outlet at the top
end of the after-drying-zone, a recirculatingcon
' duit connected to said vaporoutlet, a second vfan _ 7
shaft inicountercurrent to the descending peat a 40 having its suction side connected to said-recir
hot gas current ‘containing superheated water
culating conduit, a branch conduit leading from
vaporat a temperature below the carbonizing
the pressure side of said second fan directly into
7» temperature of the peat, and passing through the
said shaft at the bottom of the after-drying zone,
third carbonizing zone of said shaft below said
‘ av superheater, ‘and a second branch conduit
through the next lower after-drying zone of, said
7
afteredrying zone a hot gas current containing‘ 457 leading from the pressure side of said second fan
superheated water vapor at a temperature above
. the ‘carbonizing temperature of the peat.
'
‘ V 2; ' In a method as claimed in claim 1, the steps
of -.c_ontinuously withdrawinga gas stream from
the top of saidjafter-drying zone, recirculating
partof said stream directly into the bottom of
the’ after-drying zone, superheating another part
of said stream, and recirculating the superheated
part into the bottom of the carbonizing zone, A ._
V
In a method as claimed in claim 1,.the steps
through. said superheateriinto said shaft at the
bottomof said carbonizing zone. 7
>
'
8. Apparatus as claimed in:claim 7, in which‘
‘ 7 saidvapor discharge conduit includes a portion’
arranged in heat-exchange‘ relationship relative
to said air conduit,
'
v
V r
9; Apparatus as claimed inrclaim 7, in which
said superheater includes a furnace and a' con-g
duit connects the flue of’ said furnace to the suc-_
tion part of said air conduit.
of continuously withdrawing a gas ‘stream from
10. Apparatus as claimed in claim '7, in which
the column of peat at the top of the after-drying
said shaft includes a cooling zone near its bot
zone, recirculating: part of said, gas stream direct;
tom, an inlet port for a cooling gas into said.
ly into the bottom of'the after-drying zone,v
cooling zone 'of said shaft, and a conduit having
superheating another part of said gas stream, re 60 one end connected to'the cooling zone of said
circulating the superheated part‘ into the bottom
shaft'at a point'remote from said inlet and'its
of the carbonizing zone, continuously withdraw-7‘
opposite end opening into said air conduit.
ing a second gas‘ streamfrom the column of peat
11. Apparatus according to claim '7, including
at the top of the after-drying zone,- and utilizing
a third branch conduit. leading from the pressure
said second‘gas stream to heat the gas current 65 side of said second fan into said shaftbelow said
V to be passed throughthe predrying zone.
carbonizing zone.
‘
"
4. In a method’ as claimed in claim 1, the steps
of continuously withdrawing a gas stream from
cLAiis-WrLHELM PILO. '
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