Solvent removal using a condensable heat transfer vapor

Claim 2

A process for the removal of a non-aqueous liquid from a web material impregnated or coated with same, comprising contacting the web material with an effective amount of a condensable, heat transfer vapor which condenses at least in part upon the web in an amount sufficient to provide substantially all of the energy for removal of the non-aqueous liquid, with the contact being conducted countercurrent fashion, and with the amount of heat transfer vapor employed being at least 50% by weight of the non-aqueous liquid.

Claim 3

The process of claim 1, wherein the heat transfer vapor comprises saturated steam.

Claim 4

The process of claim 2, wherein the excess saturated steam in mixture with removed non-aqueous solvent vapor is passed to a recovery apparatus to recover the liquid.

Claim 5

The process of claim 3, wherein the chamber configuration is such as to induce turbulent vapor flow.

Claim 6

The process of claim 3, wherein the process is conducted in a thermally insulated chamber and the temperature of the excess saturated steam in mixture with removed non-aqueous solvent vapor is monitored as the mixture exits the chamber.

Claim 7

The process of claim 5, wherein the quantity of steam supplied to the chamber is regulated in response to the temperature monitor.

Claim 8

The process of claim 2, wherein the web material is a cellulosic substrate.

Claim 9

The process of claim 7, wherein the web material is a paper web coated with a solvent soluble resin with low water tolerance and the non-aqueous liquid removed from said paper is the organic solvent employed in impregnating the paper with the resin.

Claim 10

The process of claim 8, wherein the organic solvent is methanol.

Claim 11

The process of claim 8, wherein the resin is a phenolic resin or polyvinyl acetate resin.

Claim 12

The process of claim 2, further comprising passing the substrate contacted with the heat transfer vapor, after the contacting is complete, to a hot air oven in order to evaporate condensed steam.

Claim 13

The process of claim 11, wherein the web material is a cellulosic substrate.

Claim 14

The process of claim 12, wherein the web material is a paper coated with phenolic resin or polyvinyl acetate resin and the non-aqueous liquid removed from the paper is the organic solvent employed in impregnating the paper with the resin.

Claim 15

The process of claim 13, wherein the organic solvent is methanol.

Claim 16

The process of claim 1, wherein the heat transfer vapor consists essentially of saturated steam.

Claim 17

The process of claim 1, wherein the amount of heat transfer vapor employed is at least 65% by weight of the non-aqueous liquid.

Claim 18

The process of claim 1, wherein the contacting is conducted in a thermally insulated chamber.

Claim 19

A process for impregnating a paper with a resin which comprises: (1) contacting the paper with a solution comprising said resin dissolved in an organic solvent, and (2) removing the organic solvent from the paper by contacting the paper with a heat transfer vapor comprising saturated steam in countercurrent fashion, with the amount of saturated steam employed being at least 50% by weight of the organic solvent in the paper, and with the steam condensing at least in part upon the paper in an amount sufficient to provide substantially all of the energy for removal of the organic solvent.

Claim 20

A process for impregnating a paper with a resin which comprises: (1) contacting the paper with a solution comprising said resin dissolved in an organic solvent, and (2) removing the organic solvent from the paper by contacting the paper with a heat transfer vapor comprising saturated steam in countercurrent fashion, with the amount of saturated steam employed being at least 50% by weight of the organic solvent in the paper, and with the steam condensing at least in part upon the paper in an amount sufficient to provide substantially all of the energy for removal of the organic solvent.

Claim 21

The process of claim 18, wherein the resin is a phenolic resin or polyvinyl acetate resin and the organic solvent is an alcohol.

Claim 22

The process of claim 19, wherein the organic solvent is methanol.

Claim 23

The process of claim 18, wherein excess saturated steam in mixture with organic solvent removed from the paper is passed to a separation unit in order to recover the solvent.

Claim 24

The process of claim 21, wherein the process is conducted in a thermally insulated chamber and the temperature of the excess saturated steam in mixture with organic solvent is monitored as the mixture exits the chamber.

Claim 25

The process of claim 22, wherein the quantity of steam supplied to the chamber is regulated in response to the temperature monitor.

Claim 26

The process of claim 18, further comprising passing the paper upon completion of the contacting with the saturated steam heat transfer vapor through a hot air oven in order to evaporate condensed steam.

Claim 27

A process for the removal of a non-aqueous liquid from a web material impregnated or coated with same, comprising contacting the web material with an effective amount of a condensable, heat transfer vapor comprising saturated steam which condenses at least in part upon the web to provide energy for removal of the non-aqueous liquid, with the contact being conducted in counter-current fashion, and with the amount of saturated steam employed being at least 50% by weight of the non-aqueous liquid, conducting the process in a thermally insulated chamber, and passing excess saturated steam in mixture with removed non-aqueous solvent vapor to a recovery apparatus to recover the liquid, with the temperature of the excess saturated steam in mixture with removed non-aqueous solvent vapor being monitored as the mixture exits the chamber.

Claim 28

A process for the removal of a non-aqueous liquid from a web material impregnated or coated with same, comprising contacting the web material with an effective amount of a condensable, heat transfer vapor comprising saturated steam which condenses at least in part upon the web to provide energy for removal of the non-aqueous liquid, with the contact being conducted in counter-current fashion, and with the amount of saturated steam employed being at least 50% by weight of the non-aqueous liquid, conducting the process in a thermally insulated chamber, and passing excess saturated steam in mixture with removed non-aqueous solvent vapor to a recovery apparatus to recover the liquid, with the temperature of the excess saturated steam in mixture with removed non-aqueous solvent vapor being monitored as the mixture exits the chamber.

Claim 29

The process of claim 25, wherein the quantity of steam supplied to the chamber is regulated in response to the temperature monitor.

Claim 30

A process for impregnating a paper with a resin which comprises: (1) contacting the paper with a solution comprising said resin dissolved in an organic solvent, (2) removing the organic solvent from the paper by contacting the paper with a heat transfer vapor comprising saturated steam in counter-current fashion, the amount of saturated steam employed being at least 50% by weight of the organic solvent in the paper, and with the steam condensing at least in part upon the paper to provide energy for removal of the organic solvent, (3) conducting the process in a thermally insulated chamber, and (4) passing excess saturated steam in mixture with organic solvent removed from the paper to a separation unit in order to recover the solvent, with the temperature of the excess saturated steam in mixture with organic solvent being monitored as the mixture exits the chamber.

Claim 31

A process for impregnating a paper with a resin which comprises: (1) contacting the paper with a solution comprising said resin dissolved in an organic solvent, (2) removing the organic solvent from the paper by contacting the paper with a heat transfer vapor comprising saturated steam in counter-current fashion, the amount of saturated steam employed being at least 50% by weight of the organic solvent in the paper, and with the steam condensing at least in part upon the paper to provide energy for removal of the organic solvent, (3) conducting the process in a thermally insulated chamber, and (4) passing excess saturated steam in mixture with organic solvent removed from the paper to a separation unit in order to recover the solvent, with the temperature of the excess saturated steam in mixture with organic solvent being monitored as the mixture exits the chamber.

Claim 32

The process of claim 27, wherein the quantity of steam supplied to the chamber is regulated in response to the temperature monitor.