Patent US4764607A successfully refreshed from Google Patents.
US4764607A
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Method for recovering caprolactam
Assignee: Honeywell International Inc
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Filing: 1986-12-22
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Granted: 1988-08-16
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Expires: 2006-12-22
Abstract
Abstract Method and improved apparatus for recovering a volatile organic material, such as caprolactam, from a liquid mixture of organic and inorganic materials are disclosed. The method features the step of mixing the liquid mixture with superheated steam for 0.005 to 1.0 second to vaporize a large portion of the volatile organic material without degrading the organic materials. The steam and vaporized organic materials are then separated from the liquid mixture remaining, followed by separation of the vaporized organic material from the steam. The vaporized organic material subsequently is condensed. The improved apparatus features means for introducing superheated steam into a vaporizer feed pipe, as well as means for mixing the superheated steam with the liquid mixture in the pipe for 0.005 to 1.0 second so that a large portion of the volatile organic material is vaporized and feeds with the steam and remaining liquid mixture into the vaporizer for separation.
Inventors
- 👤 Laszlo J. Balint
- 👤 Julius Greenburg
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 21:42
CPC Classifications
C; C07; C07D; C07D201/00; C07D201/16
Claims Analysis
Total Claims: 21
Claim 1
Independent Claim
74 words
A method of recovering a volatile organic material from a liquid mixture comprising the steps of: a. mixing the liquid mixture with superheated steam for 0.005 to 1.0 second to vaporize a large portion of the volatile organic material without degrading the organic materials; b. separating the vaporized organic material and the steam from the liquid mixture remaining; c. separating the vaporized organic material from the steam; and d. condensing the vaporized organic material.
Claim 2
Independent Claim
74 words
A method of recovering a volatile organic material from a liquid mixture comprising the steps of: a. mixing the liquid mixture with superheated steam for 0.005 to 1.0 second to vaporize a large portion of the volatile organic material without degrading the organic materials; b. separating the vaporized organic material and the steam from the liquid mixture remaining; c. separating the vaporized organic material from the steam; and d. condensing the vaporized organic material.
Claim 3
Dependent Claim
12 words
The method of claim 1 wherein the volatile organic material is caprolactam.
Claim 4
Dependent Claim
22 words
The method of claim 1 wherein the liquid mixture and the superheated steam have a contact time of 0.01 to 0.10 second.
Claim 5
Dependent Claim
18 words
The method of claim 1 wherein the superheated steam is at a temperature of 400 to 600° C.
Claim 6
Dependent Claim
18 words
The method of claim 4 wherein the superheated steam is at a temperature of 450° to 550° C.
Claim 7
Dependent Claim
25 words
The method of claim 4 wherein the superheated steam is fed at a rate that is 0.5 to 2.0 times that of the liquid mixture.
Claim 8
Dependent Claim
85 words
In a method of recovering caprolactam from a liquid mixture wherein the liquid mixture is fed through a pipe to a vaporizer, the improvement comprising: a. mixing the liquid mixture with superheated steam in the pipe prior to entry into the vaporizer for 0.005 to 1.0 second to vaporize a large portion of the caprolactam; b. separating the vaporized caprolactam and the steam from the liquid mixture remaining in the vaporizer; c. separating the vaporized caprolactam from the steam; and d. condensing the vaporized caprolactam.
Claim 9
Dependent Claim
85 words
In a method of recovering caprolactam from a liquid mixture wherein the liquid mixture is fed through a pipe to a vaporizer, the improvement comprising: a. mixing the liquid mixture with superheated steam in the pipe prior to entry into the vaporizer for 0.005 to 1.0 second to vaporize a large portion of the caprolactam; b. separating the vaporized caprolactam and the steam from the liquid mixture remaining in the vaporizer; c. separating the vaporized caprolactam from the steam; and d. condensing the vaporized caprolactam.
Claim 10
Dependent Claim
22 words
The method of claim 7 wherein the liquid mixture and the superheated steam have a contact time of 0.01 to 0.10 second.
Claim 11
Dependent Claim
21 words
The method of claim 7 additionally comprising the step of sparging superheated steam through the remaining liquid mixture in the vaporizer.
Claim 12
Dependent Claim
18 words
The method of claim 7 wherein the superheated steam is at a temperature of 400 to 600° C.
Claim 13
Dependent Claim
25 words
The method of claim 10 wherein the superheated steam is fed at a rate that is 0.5 to 2.0 times that of the liquid mixture.
Claim 14
Dependent Claim
47 words
The method of claim 11 wherein the liquid mixture comprises about 25 to 70 weight percent caprolactam; the liquid mixture and the superheated steam have a contact time of 0.01 to 0.10 second; and wherein the superheated steam is at a temperature of 450 to 650° C.
Claim 15
Dependent Claim
17 words
The method of claim 12 wherein the liquid mixture comprises about 40 to 60 weight percent caprolactam.
Claim 16
Dependent Claim
103 words
In a system for recovering a volatile organic material from a liquid mixture, said system comprising a pipe for feeding the liquid mixture into a vaporizer which further comprises an exhaust for removal of vaporized material and an outlet for the discharge of unvaporized material, the improvement comprising: a. means for introducing superheated steam into the pipe; and b. means for mixing the superheated steam with the liquid mixture in the pipe for 0.005 to 1.0 second; so that a large portion of the volatile organic material is vaporized and feeds with the steam and remaining liquid mixture into the vaporizer for separation.
Claim 17
Dependent Claim
103 words
In a system for recovering a volatile organic material from a liquid mixture, said system comprising a pipe for feeding the liquid mixture into a vaporizer which further comprises an exhaust for removal of vaporized material and an outlet for the discharge of unvaporized material, the improvement comprising: a. means for introducing superheated steam into the pipe; and b. means for mixing the superheated steam with the liquid mixture in the pipe for 0.005 to 1.0 second; so that a large portion of the volatile organic material is vaporized and feeds with the steam and remaining liquid mixture into the vaporizer for separation.
Claim 18
Dependent Claim
38 words
The improved system of claim 14 further comprising a baffle, said baffle being located inside said vaporizer such that the vaporized material, the steam and the remaining liquid mixture discharge from the pipe to impinge upon the baffle.
Claim 19
Dependent Claim
18 words
The improved system of claim 14 wherein said means for mixing comprises a plurality of static mixing elements.
Claim 20
Dependent Claim
15 words
The improved system of claim 14 wherein said means for mixing comprises a mixing eductor.
Claim 21
Dependent Claim
15 words
The improved system of claim 14 wherein said means for mixing comprises a channel spiral.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-08-16 | 1992-02-15 | 1992-08-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-08-16 | 1996-02-15 | 1996-08-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-08-16 | 2000-02-15 | 2000-08-16 | $7700.00 | Window Closed / Lapsed |