Patent US4421532A successfully refreshed from Google Patents.
US4421532A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for removing and recovering volatile organic substances from industrial waste gases
Assignee: Individual
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Filing: 1981-07-27
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Granted: 1983-12-20
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Expires: 2001-07-27
Abstract
Abstract A process for removing and recovering volatile organic substances from industrial waste gases by adsorption on to solid adsorbents and desorption by hot inert gas circulating in a closed cycle, carried out continuously or intermittently. According to the new process, the volatile organic substances are recovered from the inert desorption gas partly by condensation by means of cooling, and partly by readsorption on to solid adsorbents.
Inventors
- 👤 Massimo Sacchetti
- 👤 Giovanni Aguzzi
- 👤 Gianvittorio Bianchi
- 👤 Giuseppe Caroprese
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 08:58
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/02; B01D53/04; B01D2257/00; B01D2257/70; B01D2257/708; B01D2259/00; B01D2259/40; B01D2259/40083; B01D2259/40088; B01D2259/4009; B01D2259/403
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
227 words
A process for removing and recovering a volatile organic substance from an industrial waste gas comprising (1) passing an industrial waste gas containing a volatile organic substance over a solid adsorbent for said volatile organic substance to adsorb said volatile organic substance therein, (2) desorbing the sorbed solid adsorbent with a hot steam-free inert desorption gas circulating in a closed cycle, the desorbing operation comprising the steps of: (a) heating a steam-free inert desorption gas, (b) circulating the heated steam-free inert desorption gas through the sorbed solid adsorbent to be regenerated, (c) cooling the circulated desorption gas now enriched with said volatile organic substance at a temperature suitable for condensation of most of said organic substance to form a condensate, (d) separating said condensate from the remaining circulated desorption gas, (e) purifying the desorption gas by passing said gas through the same adsorbent through which said industrial waste gas has passed in the adsorption step (1), said adsorbent being regenerated with the same desorption gas circulating in a closed cycle, and (f) recycling the purified desorption gas to heating step (a), and (3) recovering a portion of said volatile organic substance by cooling said hot steam-free inert desorption gas containing said volatile organic substance and recovering the remainder of said volatile organic substance by readsorbing said volatile organic substance in said inert gas on said solid adsorbent.
Claim 2
Dependent Claim
227 words
A process for removing and recovering a volatile organic substance from an industrial waste gas comprising (1) passing an industrial waste gas containing a volatile organic substance over a solid adsorbent for said volatile organic substance to adsorb said volatile organic substance therein, (2) desorbing the sorbed solid adsorbent with a hot steam-free inert desorption gas circulating in a closed cycle, the desorbing operation comprising the steps of: (a) heating a steam-free inert desorption gas, (b) circulating the heated steam-free inert desorption gas through the sorbed solid adsorbent to be regenerated, (c) cooling the circulated desorption gas now enriched with said volatile organic substance at a temperature suitable for condensation of most of said organic substance to form a condensate, (d) separating said condensate from the remaining circulated desorption gas, (e) purifying the desorption gas by passing said gas through the same adsorbent through which said industrial waste gas has passed in the adsorption step (1), said adsorbent being regenerated with the same desorption gas circulating in a closed cycle, and (f) recycling the purified desorption gas to heating step (a), and (3) recovering a portion of said volatile organic substance by cooling said hot steam-free inert desorption gas containing said volatile organic substance and recovering the remainder of said volatile organic substance by readsorbing said volatile organic substance in said inert gas on said solid adsorbent.
Claim 3
Dependent Claim
14 words
A process according to claim 1, wherein the desorption is facilitated by applying vacuum.
Claim 4
Dependent Claim
20 words
A process according to claim 1, wherein the solid adsorbent is granular activated carbon, and the inert gas is nitrogen.
Claim 5
Dependent Claim
24 words
A process according to claim 1, wherein the desorption is carried out with inert gases before feeding volatile organic substances to the solid adsorbent.
Claim 6
Dependent Claim
31 words
A process according to claim 1, wherein the desorption is carried out with inert gas heated by means of heat sources immersed in the solid adsorbent loaded with volatile organic substances.
Claim 7
Dependent Claim
48 words
The process of claim 1, wherein purification of the desorption gas is carried out by passing said gas through at least one adsorbent provided at the outlet of the condensation/separation system, said at least one adsorbent being regenerated with the same desorption gas circulating in a closed cycle.
Claim 8
Dependent Claim
21 words
The process of claim 1, further comprising cooling the regenerated solid adsorbent with purified desorption gas before said gas is heated.
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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 |