Method and apparatus for oxygen delignification

Claim 2

A process for the continuous oxygen delignification of pulp comprising the steps of introducing pulp at from 8-20% consistency and alkaline chemicals into a substantially horizontal tubular reaction zone while maintaining a gas space at the top of said reaction zone, adding oxygen gas into said zone at a point adjacent the introduction of said pulp, said oxygen gas moving freely through said reaction zone in substantially plug flow, continuously mixing and transporting the mixture of pulp and alkaline chemicals along the entire length of said reaction zone in substantially plug flow concurrently with said oxygen gas in said gas space through the reaction zone, the pulp level in said reaction zone being no more than 90% of the total volume of said reaction zone and removing the delignified pulp through an outlet in said zone.

Claim 3

The process of claim 1 including the step of withdrawing gas containing delignification reaction product gases from a point adjacent said outlet.

Claim 4

A process for the continuous oxygen delignification of pulp comprising the steps of introducing pulp at from 8-20% consistency and alkaline chemicals into a first substantially horizontal tubular reaction zone while maintaining a gas space at the top of said reaction zone, adding oxygen gas into said first zone at a point adjacent the introduction of said pulp, said oxygen gas moving freely through said first reaction zone is substantially plug flow, continuously mixing and transporting the mixture of pulp and alkaline chemicals along the entire length of said first reacton zone in substantially plug flow concurrently with said oxygen gas in said gas space through said first reaction zone, the pulp level in said reaction zone being no more than 90% of the total volume of said first reaction zone, transferring said mixture into one of more subsequent substantially horizontal, tubular reaction zones, transporting the mixture of pulp and alkaline chemicals in substatially plug flow concurrently with said oxygen gas through said one or more subsequent zones, and removing delignified pulp through an outlet in the last of said one or more subsequent zones.

Claim 5

A process for the continuous oxygen delignification of pulp comprising the steps of introducing pulp at from 8-20% consistency and alkaline chemicals into a first substantially horizontal tubular reaction zone while maintaining a gas space at the top of said reaction zone, adding oxygen gas into said first zone at a point adjacent the introduction of said pulp, said oxygen gas moving freely through said first reaction zone is substantially plug flow, continuously mixing and transporting the mixture of pulp and alkaline chemicals along the entire length of said first reacton zone in substantially plug flow concurrently with said oxygen gas in said gas space through said first reaction zone, the pulp level in said reaction zone being no more than 90% of the total volume of said first reaction zone, transferring said mixture into one of more subsequent substantially horizontal, tubular reaction zones, transporting the mixture of pulp and alkaline chemicals in substatially plug flow concurrently with said oxygen gas through said one or more subsequent zones, and removing delignified pulp through an outlet in the last of said one or more subsequent zones.

Claim 6

The process of claim 3 including the step of withdrawing gas containing reaction product gases from a point adjacent said outlet.

Claim 7

The process of claim 4 including the steps of catalytically oxidizing the potentially combustible reaction product gases withdrawn from the last reaction zone and recirculating the withdrawn gas to a point adjacent the inlet of the last of said one or more subsequent reaction zones.

Claim 8

The process of claim 4 including the steps of cooling the gas withdrawn from the last reacton zone and recirculating the cooled gas to a point adjacent the inlet of the last of said one or more subsequent reaction zones.

Claim 9

The process of claim 4 including the steps of withdrawing gas containing reaction product gases from points adjacent the outlets of each of said one or more subsequent reaction zones, catalytically oxidizing the potentially combustible reaction product gases withdrawn from each of said zones, and recirculating the withdrawn gas to points adjacent the respective inlets of each of said one or more subsequent reaction zones.

Claim 10

The process of claim 4 including the steps of cooling the gas withdrawn from points adjacent the outlets of each of said one or more subsequent reaction zones and recirculating the cooled gas to points adjacent the respective inlets of each of said one or more subsequent reaction zones.

Claim 11

The process of claim 5 including the step of cooling the gas withdrawn from said last reaction zone prior to recirculating it.

Claim 12

The process of claim 7 including the step of cooling the gases withdrawn from each of said one or more subsequent reaction zones prior to recirculating them.

Claim 13

A process for the continuous oxygen delignification of pulp comprising the steps of introducing pulp at from 8-20% consistency and alkaline chemicals into a first end of a substantially horizontal tubular reaction zone while maintaining a gas space at the top of said reaction zone, adding oxygen gas into said reaction zone at the opposite end of said reaction zone, said oxygen gas moving freely through said reaction zone in substantially plug flow, continuously mixing and transporting the mixture of pulp and alkaline chemicals along the entire length of said reaction zone in substantially plug flow countercurrently to the direction of flow of said oxygen as in said gas space through the reaction zone, the pulp level in said reaction zone being no more than 90% of the total volume of said reaction zone, and removing the delignified pulp through an outlet at said opposite end of said zone.

Claim 14

A process for the continuous oxygen delignification of pulp comprising the steps of introducing pulp at from 8-20% consistency and alkaline chemicals into a first end of a substantially horizontal tubular reaction zone while maintaining a gas space at the top of said reaction zone, adding oxygen gas into said reaction zone at the opposite end of said reaction zone, said oxygen gas moving freely through said reaction zone in substantially plug flow, continuously mixing and transporting the mixture of pulp and alkaline chemicals along the entire length of said reaction zone in substantially plug flow countercurrently to the direction of flow of said oxygen as in said gas space through the reaction zone, the pulp level in said reaction zone being no more than 90% of the total volume of said reaction zone, and removing the delignified pulp through an outlet at said opposite end of said zone.

Claim 15

The process of claim 11 including the step of withdrawing gas containing delignification reaction product gases from a point adjacent said first end of said zone.

Claim 16

A process for the continuous oxygen delignification of pulp comprising the steps of introducing pulp at from 8-20% consistency and alkaline chemicals into a first end of a substantially horizontal tubular reaction zone while maintaining a gas space at the top of said reaction zone, adding oxygen gas into said zone, said oxygen gas moving freely through said reaction zone in substantially plug flow, continuously mixing and transporting the mixture of pulp and alkaline chemicals along the entire length of said reaction zone in substantially plug flow from said first end of said reaction zone to the opposite end thereof, directing a first portion of said oxygen gas to flow in said gas space substantially concurrently with the direction of flow of said mixture while directing a second portion of said oxygen gas to flow in said gas space countercurrently to the direction of flow of said mixture, the pulp level in said reaction zone being no more than 90% of the total volume of said reaction zone, and removing the delignified pulp through an outlet at said opposite end of said zone.

Claim 17

A process for the continuous oxygen delignification of pulp comprising the steps of introducing pulp at from 8-20% consistency and alkaline chemicals into a first end of a substantially horizontal tubular reaction zone while maintaining a gas space at the top of said reaction zone, adding oxygen gas into said zone, said oxygen gas moving freely through said reaction zone in substantially plug flow, continuously mixing and transporting the mixture of pulp and alkaline chemicals along the entire length of said reaction zone in substantially plug flow from said first end of said reaction zone to the opposite end thereof, directing a first portion of said oxygen gas to flow in said gas space substantially concurrently with the direction of flow of said mixture while directing a second portion of said oxygen gas to flow in said gas space countercurrently to the direction of flow of said mixture, the pulp level in said reaction zone being no more than 90% of the total volume of said reaction zone, and removing the delignified pulp through an outlet at said opposite end of said zone.

Claim 18

Apparatus for continuous oxygen delignification of pulp comprising in combination: (a) a first substantially horizontal, tubular reaction vessel having an inlet and an outlet, (b) means for introducing pulp at from 8-20% consistency at said inlet at a first end of said first reaction vessel while maintaining a gas space at the top of said vessel, (c) means for introducing oxygen gas into said reaction vessel at at least one point adjacent to said means for introducing pulp for concurrent flow of said gas in said gas space with said pulp, (d) means in said reaction vessel for transporting pulp from said first end of said reaction vessel to the opposite end thereof, (e) means for withdrawing delignified pulp from said outlet at said opposite end of said first reaction vessel, (f) a second, substantially horizontal, tubular reaction vessel having an inlet and an outlet, said inlet in fluid communication with the outlet of said first reacton vessel, (g) said second tubular reaction vessel including means for transferring pulp to a first end of said second reaction vessel through said inlet, (h) means in said second reaction vessel for transporting said pulp from said first end of said reaction vessel to the outlet at the opposite end thereof, (i) means for withdrawing delignified pulp from the outlet at said opposite end of said second reaction vessel, (j) means in said second reaction vessel for withdrawing gas containing reaction product gases at a point adjacent said opposite end of said second reaction vessel, (k) means for recirculating the withdrawn gas to said first end of said second reaction vessel, said recirculating means including a generally upwardly inclined conduit means connecting said means for withdrawing gas with said outlet of said first reaction vessel, said recirculating means further including means for catalytically oxidizing potentially combustible reaction gases.

Claim 19

Apparatus for continuous oxygen delignification of pulp comprising in combination: (a) a first substantially horizontal, tubular reaction vessel having an inlet and an outlet, (b) means for introducing pulp at from 8-20% consistency at said inlet at a first end of said first reaction vessel while maintaining a gas space at the top of said vessel, (c) means for introducing oxygen gas into said reaction vessel at at least one point adjacent to said means for introducing pulp for concurrent flow of said gas in said gas space with said pulp, (d) means in said reaction vessel for transporting pulp from said first end of said reaction vessel to the opposite end thereof, (e) means for withdrawing delignified pulp from said outlet at said opposite end of said first reaction vessel, (f) a second, substantially horizontal, tubular reaction vessel having an inlet and an outlet, said inlet in fluid communication with the outlet of said first reacton vessel, (g) said second tubular reaction vessel including means for transferring pulp to a first end of said second reaction vessel through said inlet, (h) means in said second reaction vessel for transporting said pulp from said first end of said reaction vessel to the outlet at the opposite end thereof, (i) means for withdrawing delignified pulp from the outlet at said opposite end of said second reaction vessel, (j) means in said second reaction vessel for withdrawing gas containing reaction product gases at a point adjacent said opposite end of said second reaction vessel, (k) means for recirculating the withdrawn gas to said first end of said second reaction vessel, said recirculating means including a generally upwardly inclined conduit means connecting said means for withdrawing gas with said outlet of said first reaction vessel, said recirculating means further including means for catalytically oxidizing potentially combustible reaction gases.