US5695546A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for collecting volatile organic substances
Assignee: Mitsubishi Heavy Industries Ltd
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Filing: 1996-05-08
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Granted: 1997-12-09
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Expires: 2016-05-08
Abstract
Abstract A method for collecting volatile organic substances from off-gas containing moisture and volatile organic substances. After the moisture has been removed by a dehumidifying tower filled with moisture absorbent for selectively adsorbing the moisture from the gas containing the organic substances and the moisture, the organic substances are adsorbed and removed under a relatively low temperature condition. The organic substances is desorbed under a relatively high temperature condition from the adsorbing tower which is saturated with the organic substances. The desorbed organic substances are liquefied and collected under a low temperature and/or pressurizing condition. The dry gas from which the organic substances have been removed and made harmless is heated if necessary. Thereafter, the dry gas is purged in a counter flow manner in the dehumidifying tower which is saturated with the moisture to perform the regeneration of the moisture absorbent and is discharged to the outside of the system together with the desorbed moisture.
Inventors
- 👤 Jun Izumi
- 👤 Akinori Yasutake
- 👤 Hiroyuki Tsutaya
- 👤 Takayuki Harada
- 👤 Kenichi Hamada
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 09:35
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/26; B01D53/261; B01D53/02; B01D53/06; B01J; B01J20/00; B01J20/02; B01J20/06; B01J20/08; B01J20/10; B01J20/103; B01D2253/00; B01D2253/10; B01D2253/106; B01D2253/108; B01D2253/30; B01D2253/34; B01D2253/342; B01D2253/3425; B01D2257/00; B01D2257/70; B01D2257/80; B01D53/04; B01D53/0462; B01D53/047
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
257 words
A method for collecting the volatile organic substances by processing gas containing volatile organic substances and moisture with moisture absorbent and another adsorbent, comprising the following steps of: introducing the gas containing the volatile organic substances and the moisture into a dehumidifying tower filled with the moisture absorbent for selectively adsorbing the moisture and being in a dehydrating process under a relatively low temperature condition to remove the moisture, and thereafter causing the gas to flow through an adsorbing tower filled with said another adsorbent and being in an adsorbing process under a relatively low temperature condition to adsorb and remove the volatile organic substances; desorbing the adsorbed moisture, by causing the gas from which the moisture and the volatile organic substances have been removed, to pass through the dehumidifying tower being in a moisture absorbent regenerating process under a relatively high temperature condition, and discharging the gas outside the system together with the desorbed moisture; causing a high concentration volatile organic substances containing gas the volatile organic substances adsorbed by causing part of the gas from which the moisture and the volatile organic substances have been removed, to pass through the adsorbing tower being in the removal process under a relatively high temperature condition; introducing the high concentration volatile organic substances containing gas into a liquefier, cooling and/or pressurizing the gas to be liquefied to collect the volatile organic substances; and returning the gas from which the volatile organic substances have been separated in the liquefier, back to the adsorbing process for the volatile organic substances.
Claim 2
Independent Claim
257 words
A method for collecting the volatile organic substances by processing gas containing volatile organic substances and moisture with moisture absorbent and another adsorbent, comprising the following steps of: introducing the gas containing the volatile organic substances and the moisture into a dehumidifying tower filled with the moisture absorbent for selectively adsorbing the moisture and being in a dehydrating process under a relatively low temperature condition to remove the moisture, and thereafter causing the gas to flow through an adsorbing tower filled with said another adsorbent and being in an adsorbing process under a relatively low temperature condition to adsorb and remove the volatile organic substances; desorbing the adsorbed moisture, by causing the gas from which the moisture and the volatile organic substances have been removed, to pass through the dehumidifying tower being in a moisture absorbent regenerating process under a relatively high temperature condition, and discharging the gas outside the system together with the desorbed moisture; causing a high concentration volatile organic substances containing gas the volatile organic substances adsorbed by causing part of the gas from which the moisture and the volatile organic substances have been removed, to pass through the adsorbing tower being in the removal process under a relatively high temperature condition; introducing the high concentration volatile organic substances containing gas into a liquefier, cooling and/or pressurizing the gas to be liquefied to collect the volatile organic substances; and returning the gas from which the volatile organic substances have been separated in the liquefier, back to the adsorbing process for the volatile organic substances.
Claim 3
Dependent Claim
111 words
The method for collecting volatile organic substances according to claim 1, wherein said relatively low temperature condition relating to the dehydrating process in the dehumidifying tower is in the range of 10° to 50° C., said relatively high temperature condition relating to the moisture absorbent regenerating process is in the range of 35° to 125° C., said relatively low temperature condition relating to the adsorbing process in the adsorbing tower for the organic substances is in the range of -30° to 10° C., and the relatively high temperature condition relating to the removal process for the organic substances for the organic substances is in the range of 35° to 125° C.
Claim 4
Dependent Claim
45 words
The method for collecting volatile organic substances according to claim 1 or 2, wherein the dry gas which is downstream of said adsorbing tower being in the adsorbing process is used as a regenerating gas in the moisture absorbent regenerating process in said dehumidifying tower.
Claim 5
Dependent Claim
34 words
The method for collecting volatile organic substances according to claim 2, wherein an adsorbent having a silica/alumina ratio of 25 or more is used as said other adsorbent for adsorbing the volatile organic substances.
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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) | 2000-12-08 | 2001-06-09 | 2001-12-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2004-12-08 | 2005-06-09 | 2005-12-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2008-12-08 | 2009-06-09 | 2009-12-09 | $7700.00 | Window Closed / Lapsed |