Process and apparatus for flash drying fluffed cellulose pulp

Claim 2

In the process for the flash drying of particulate cellulose pulp, comprising the steps (1) entraining the pulp particles in a gas, (2) establishing and maintaining a flow of the gas-particulate cellulose pulp mixture along a confined path, (3) transferring heat into the gas-particulate cellulose pulp mixture in a heat-transfer zone along the path, and (4) repeating step (3) in a successive series of heat-transfer zones, the improvement which comprises employing as the carrier gas steam under a pressure of at least 0.12 to 0.15 MPa; supplying heat to the heat-transfer zone as heating steam whose saturation pressure exceeds the pressure of the carrier steam; and then separating the fluffed cellulose pulp and carrier steam.

Claim 3

The process as claimed in claim 1, wherein the pressure of the carrier steam is at least 0.2 to 0.4 MPa.

Claim 4

The process as claimed in claim 1, wherein the fluffed cellulose pulp and the steam are in a ratio not greater than about 0.35 kg dry weight of pulp to 1.0 kg of steam.

Claim 5

The process as claimed in claim 1, wherein after separation part of the carrier steam is recycled, for reuse as carrier steam.

Claim 6

The process as claimed in claim 1, wherein after separation part of the carrier steam is used for drying of paper at a pressure of from 0.2 to 0.5 MPa.

Claim 7

The process as claimed in claim 1, wherein the carrier steam is superheated to a temperature within the range from about 120° C to about 190° C prior to mixing with particulate cellulose pulp to be dried.

Claim 8

The process as claimed in claim 1, wherein the particulate cellulose pulp is dried to a solids content of up to about 60%.

Claim 9

The process as claimed in claim 1, wherein the particulate cellulose pulp is dried to a solids content of up to about 95%.

Claim 10

The process as claimed in claim 1, which comprises imparting kinetic energy to the steam-particulate cellulose pulp mixture in at least in one zone along the confined path.

Claim 11

The process as claimed in claim 9, wherein kinetic energy is imparted to the steam-particulate cellulose pulp mixture following each step and prior to each heat-transfer step.

Claim 12

Apparatus for drying particulate cellulose pulp comprising a pressure conduit system defining a confined path for a flow of particulate cellulose pulp entrained in steam; means for establishing a flow of particulate cellulose pulp entrained in steam through the conduit system; a multiplicity of heat exchangers in the conduit system for transferring heat into the steam-particulate cellulose pulp mixture in heat exchanger zones; and at least one blower in the conduit system for imparting kinetic energy to the steam-particulate cellulose pulp mixture, the conduit system including a plurality of laterally adjacent, generally parallel conduit sections comprising spaced-apart heat exchangers, heat exchanger including therewithin a plurality of generally parallel tubes carrying the steam-entrained particulate cellulose pulp and a chamber through which the tubes pass and through which heating steam can be conducted over the outsides of the tubes to heat the tubes.

Claim 13

Apparatus for drying particulate cellulose pulp comprising a pressure conduit system defining a confined path for a flow of particulate cellulose pulp entrained in steam; means for establishing a flow of particulate cellulose pulp entrained in steam through the conduit system; a multiplicity of heat exchangers in the conduit system for transferring heat into the steam-particulate cellulose pulp mixture in heat exchanger zones; and at least one blower in the conduit system for imparting kinetic energy to the steam-particulate cellulose pulp mixture, the conduit system including a plurality of laterally adjacent, generally parallel conduit sections comprising spaced-apart heat exchangers, heat exchanger including therewithin a plurality of generally parallel tubes carrying the steam-entrained particulate cellulose pulp and a chamber through which the tubes pass and through which heating steam can be conducted over the outsides of the tubes to heat the tubes.

Claim 14

Apparatus according to claim 11 comprising means for controlling the supply of particulate cellulose pulp and carrier steam to the conduit to maintain an amount of particulate cellulose pulp not greater than 0.35 kg dry weight for each 1.0 kg of carrier steam

Claim 15

Apparatus according to claim 11 comprising means for controlling the supply of heat to the heat exchangers and the superheating temperature of the carrier steam and the moisture content of the particulate cellulose pulp processed in the apparatus.

Claim 16

Apparatus as claimed in claim 11 comprising cyclone means for separation of particulate cellulose pulp and carrier steam before discharge of particulate cellulose pulp from the conduit system.

Claim 17

Apparatus as claimed in claim 11, comprising means for recycling steam used as carrier steam to the conduit system for reuse as carrier steam.