US2016024714A1PendingUtilityA1
Condenser comprising a delivery tube and method for operating a condenser
Est. expiryMar 15, 2033(~6.6 yrs left)· nominal 20-yr term from priority
Inventors:Hans-Joachim Boltersdorf
D21D 5/24D21C 5/02D21C 9/00D21B 1/345B30B 9/121B30B 9/16B30B 9/163Y02W30/64B30B 9/125D21B 1/32D21B 1/342B30B 9/166D21C 9/18B30B 9/18B30B 9/14B30B 9/12
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Claims
Abstract
A liquefier with a cylindrical delivery tube comprises a rotatable spiral disposed in the delivery tube, wherein water intakes are disposed on the delivery tube. A centrifugal pump is preferably disposed downstream of the delivery tube, said centrifugal pump delivering the liquefied medium onward.
Claims
exact text as granted — not AI-modified1 . A liquefier ( 1 ) with a delivery tube ( 2 ), which comprises an inlet ( 4 ) and an outlet ( 5 ) and in which a thick-stock conveyor ( 3 ) is disposed, wherein a centrifugal pump ( 12 ) is disposed at the outlet ( 5 ) of the delivery tube ( 2 ).
2 . The liquefier according to claim 1 , wherein a main liquid intake ( 9 ) is disposed at the outlet of the delivery tube and before the centrifugal pump.
3 . The liquefier according to claim 1 , wherein the main liquid intake has a directional component in the direction of the axis of the delivery tube ( 2 ).
4 . The liquefier according to claim 1 , wherein the main liquid intake has a directional component in the direction of a circumferential line of the delivery tube ( 2 ).
5 . The liquefier according to claim 1 , wherein a funnel ( 8 ) is disposed at the outlet ( 5 ) of the delivery tube ( 2 ).
6 . The liquefier according to claim 5 , wherein an end of the thick-stock conveyor ( 3 ), the external diameter whereof tapers corresponding to the funnel ( 8 ), is disposed in the region of the funnel ( 8 ).
7 . The liquefier according to claim 5 , wherein the centrifugal pump ( 12 ) is disposed directly at the tapered end ( 11 ) of the funnel ( 8 ).
8 . The liquefier according to claim 5 , wherein the thick-stock conveyor ( 3 ), the funnel ( 8 ) and the centrifugal pump ( 12 ) are disposed on a straight line.
9 . The liquefier according to claim 1 , wherein the thick-stock conveyor ( 3 ) is a screw.
10 . The liquefier according to claim 1 , wherein the passage width of the thick-stock conveyor ( 3 ) in the delivery tube ( 2 ) increases from the inlet ( 4 ) to the outlet ( 5 ).
11 . The liquefier according to claim 1 , wherein at the inlet ( 4 ) of the delivery tube ( 2 ), an intake ( 14 ) is disposed at right angles to the delivery direction of the thick-stock conveyor ( 3 ).
12 . The liquefier according to claim 11 , wherein the delivery tube ( 2 ) comprises a widened portion ( 16 ) at the transition from the intake ( 14 ) to the delivery tube ( 2 ).
13 . The liquefier according to claim 11 , wherein the intake ( 14 ) comprises a constriction ( 17 ) at the transition to the delivery tube ( 2 ).
14 . The liquefier according to claim 11 , wherein a dumping height measuring device ( 21 ) is disposed in the intake ( 14 ).
15 . The liquefier according to claim 11 , wherein a measuring device ( 18 ) for determining the hydrostatic pressure is disposed in the intake ( 14 ) or in the delivery tube ( 2 ).
16 . The liquefier according to claim 1 , wherein auxiliary liquid intakes ( 6 , 7 ) are disposed on the delivery tube ( 2 ).
17 . The liquefier according to claim 1 , wherein a hydrocyclone is disposed at the outlet ( 5 ) of the centrifugal pump ( 12 ) and following the latter in the flow direction.
18 . The liquefier according to claim 17 , wherein a line leads from the liquid outlet of the hydrocyclone directly before the inlet of the centrifugal pump ( 12 ).
19 . A method for operating a liquefier according to claim 1 , wherein the material to be treated is pre-treated in a solid-stock storage unit with a total stock density of more than 15% GG total stock density, the total stock density is then reduced in the liquefier ( 56 ) to less than 10% GG, preferably less than 5% GG, and the liquefied material is delivered onward with a centrifugal pump ( 12 ).
20 . The method according to claim 19 , wherein the liquefied material is delivered from the centrifugal pump ( 12 ) into a cyclone ( 66 ), preferably into a hydrocyclone, and is fractionated there.
21 . The method according to claim 20 , wherein a fraction is delivered from the cyclone ( 66 ) back into the solid-stock storage unit.
22 . The method according to claim 1 , wherein the solid-stock storage unit is a conditioner ( 30 ) with an agitator and a sieve ( 51 ), in which a fraction, such as in particular fibrous material, is separated from the material by the sieve ( 51 ).
23 . The method according to claim 22 , wherein the liquid fraction is drawn off from the cyclone ( 66 ) through a preferably polished cone.
24 . The method according to claim 1 , wherein at least 50% of the liquid is added in the region of the outlet of the delivery tube ( 2 ).
25 . The method according to claim 1 , wherein the pressure of the delivered material is measured in the liquefier ( 56 ).
26 . The method according to claim 25 , wherein during the operation of the liquefier ( 56 ), the distance between the dumping height and the height of the liquid in the liquefier ( 56 ) is measured and kept in a predetermined range.
27 . The method according to claim 25 , wherein pressurised water is added at the delivery tube ( 2 ) and/or at the outlet ( 5 ) of the delivery tube ( 2 ) and the value measured in the liquefier ( 56 ) is used to control a water intake ( 12 ) to the delivered material.
28 . The method according to claim 25 , wherein the value measured in the liquefier ( 56 ) is used to control a drive ( 19 ) of the thick-stock conveyor ( 3 ).
29 . The method according to claim 25 , wherein the value measured in the liquefier ( 56 ) is used to control a drive ( 20 ) of a pump ( 35 ) downstream of the delivery section.Join the waitlist — get patent alerts
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