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US4421532A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for removing and recovering volatile organic substances from industrial waste gases

Assignee: Individual
•
Filing: 1981-07-27
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Granted: 1983-12-20
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Expires: 2001-07-27
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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 03:33
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.

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

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