US4421794A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Solvent removal via continuously superheated heat transfer medium
Assignee: Custom Papers Group Inc
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Filing: 1981-12-18
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Granted: 1983-12-20
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Expires: 2001-12-18
Abstract
Abstract Non-aqueous solvents are removed from a substrate, e.g., paper, by contacting the substrate with a condensable, vaporous heat transfer medium that is in a superheated state, e.g., superheated steam, and maintaining said substrate in contact with said superheated heat transfer medium, while also maintaining said heat transfer medium in superheated state, for a period of time sufficient to effect removal of said non-aqueous liquid from said substrate without concomitant condensation of said superheated heat transfer medium thereon. The superheated heat transfer medium, as well as being the source of energy for evaporating the solvent, acts as a solvent vapor transport medium. Upon evaporation of the solvent, the solvent vapor-heat transfer medium mixture can be sent to a recovery zone to easily recover said solvent via condensation of the mixture and thereby avoid the discharge of said solvent vapors into the atmosphere.
Inventors
- 👤 Homan B. Kinsley, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 03:40
CPC Classifications
D; D21; D21H; D21H25/00; D21H25/04; D21H25/06; F; F26; F26B; F26B13/00; F26B13/10; F26B25/00; F26B25/005; F26B25/006
Claims Analysis
Total Claims: 24
Claim 1
Independent Claim
108 words
A process for the removal of a non-aqueous liquid from a high bulk, low density, porous cellulosic substrate having a void volume of from about 60 to 90 percent which is essentially completely impregnated with said non-aqueous liquid, comprising contacting such substrate with an effective amount of a condensable, vaporous heat transfer medium which is in a superheated state, and maintaining said substrate in contact with said superheated transfer medium, while also maintaining said heat transfer medium in superheated state, for a period of time sufficient to effect removal of substantially all said non-aqueous liquid from said substrate without concomitant condensation of said superheated heat transfer medium thereon.
Claim 2
Dependent Claim
108 words
A process for the removal of a non-aqueous liquid from a high bulk, low density, porous cellulosic substrate having a void volume of from about 60 to 90 percent which is essentially completely impregnated with said non-aqueous liquid, comprising contacting such substrate with an effective amount of a condensable, vaporous heat transfer medium which is in a superheated state, and maintaining said substrate in contact with said superheated transfer medium, while also maintaining said heat transfer medium in superheated state, for a period of time sufficient to effect removal of substantially all said non-aqueous liquid from said substrate without concomitant condensation of said superheated heat transfer medium thereon.
Claim 3
Dependent Claim
13 words
The process of claim 1 wherein said heat transfer medium is superheated steam.
Claim 4
Dependent Claim
29 words
The process of claim 2 wherein superheated steam in mixture with removed non-aqueous liquid is passed to separation to recover said liquid and said separation comprises decantation or distillation.
Claim 5
Dependent Claim
41 words
The process of claim 2 wherein said superheated steam is employed at a temperature in the range of about 500° to about 1,000° F. upon first contacting said substrate and is still in a superheated state when last contacting said substrate.
Claim 6
Dependent Claim
24 words
The process of claim 4 wherein said superheated steam is employed at a temperature in the range of about 600° to about 900° F.
Claim 7
Dependent Claim
27 words
The process of claim 4 or 5 wherein said contacting of the substrate with the superheated steam is conducted under pressure of about 5 psig or less.
Claim 8
Dependent Claim
39 words
The process of claim 4 wherein said substrate is a paper substrate coated with a phenolic resin and said non-aqueous liquid removed from said paper substrate is the organic solvent employed in impregnating the paper with the phenolic resin.
Claim 9
Dependent Claim
11 words
The process of claim 7 wherein said organic solvent is methanol.
Claim 10
Dependent Claim
57 words
The process of claim 8 wherein about 3 to about 8 lbs of superheated steam per hour are employed for every lb of methanol to be removed from the paper substrate and wherein said superheated steam is at a temperature in the range of about 600° to about 900° F. upon initial contact with said paper substrate.
Claim 11
Dependent Claim
19 words
The process of claim 9 wherein about 4 to about 6 lbs of superheated steam per hour are employed.
Claim 12
Dependent Claim
32 words
The process of claim 9 or 10 wherein the contacting of the substrate with the superheated steam is conducted under a pressure in the range of about -5 to about +5 psig.
Claim 13
Dependent Claim
37 words
The process of claim 2 wherein the amount of superheated steam employed is in the range of about 3 to about 8 lbs of superheated steam per hour for every lb of non-aqueous liquid to be removed.
Claim 14
Dependent Claim
29 words
The process of claim 2 wherein the amount of superheated steam employed is at least 3 lbs. of superheated steam for every lb. of non-aqueous liquid to be removed.
Claim 15
Dependent Claim
15 words
The process of claim 2 wherein the superheated steam passes through the porous cellulosic substrate.
Claim 16
Dependent Claim
11 words
The process of claim 1, wherein the non-aqueous liquid is methanol.
Claim 17
Dependent Claim
24 words
The process of claim 15, wherein the removal of methanol is such that the methanol content of the substrate is about 0.1% or less.
Claim 18
Dependent Claim
25 words
The process of claim 1, wherein the removal of the non-aqueous liquid is such that its content in the substrate is about 0.1% or less.
Claim 19
Dependent Claim
133 words
A process for impregnating a high bulk, porous paper substrate having a void volume of from about 60 to 90 percent with a resin which comprises (i) contacting said paper substrate with a solution comprising said resin dissolved in an organic solvent whereby the paper substrate becomes essentially completely impregnated therewith, and (ii) removing substantially all the organic solvent from the substrate by contacting said paper substrate with an effective amount of a condensable, vaporous heat transfer medium which is in a superheated state, and maintaining said paper substrate in contact with the superheated heat transfer medium, while maintaining said heat transfer medium in superheated state, for a period of time sufficient to effect said removal of said organic solvent without concomitant condensation of said superheated heat transfer medium on the paper substrate.
Claim 20
Dependent Claim
133 words
A process for impregnating a high bulk, porous paper substrate having a void volume of from about 60 to 90 percent with a resin which comprises (i) contacting said paper substrate with a solution comprising said resin dissolved in an organic solvent whereby the paper substrate becomes essentially completely impregnated therewith, and (ii) removing substantially all the organic solvent from the substrate by contacting said paper substrate with an effective amount of a condensable, vaporous heat transfer medium which is in a superheated state, and maintaining said paper substrate in contact with the superheated heat transfer medium, while maintaining said heat transfer medium in superheated state, for a period of time sufficient to effect said removal of said organic solvent without concomitant condensation of said superheated heat transfer medium on the paper substrate.
Claim 21
Dependent Claim
93 words
The process of claim 18 wherein said superheated heat transfer medium is superheated steam; said resin is a phenolic resin; said organic solvent is an alcohol; and said superheated steam is employed under a pressure in the range of about -5 to about +5 psig, at a temperature in the range of about 600° to 900° F. upon initial contact with the paper substrate, and in an amount in the range of about 3 to about 8 lbs of superheated steam per hour per lb of alcohol to be removed in said hour.
Claim 22
Dependent Claim
11 words
The process of claim 18, wherein the organic solvent is methanol.
Claim 23
Dependent Claim
10 words
The process of claim 19, wherein the alcohol is methanol.
Claim 24
Dependent Claim
25 words
The process of claim 21, wherein the removal of methanol is such that the methanol content of the paper substrate is about 0.1% or less.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-12-19 | 1987-06-20 | 1987-12-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-12-19 | 1991-06-20 | 1991-12-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-12-19 | 1995-06-20 | 1995-12-20 | $7700.00 | Window Closed / Lapsed |