US4940828A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Steam cracking feed gas saturation
Assignee: MW Kellogg Co
•
Filing: 1989-10-13
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Granted: 1990-07-10
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Expires: 2009-10-13
Abstract
Abstract Dilution steam for steam cracking hydrocarbons to produce lower olefins is economically provided by saturating gaseous hydrocarbon feed with water at a temperature selected to achieve the particular steam to hydrocarbon ratio desired in the steam cracking step. Complete saturation of the feed gas is ensured by injecting the gas into the flooded portion of an indirectly heated tubular saturation zone.
Inventors
- 👤 William C. Petterson
- 👤 Thomas A. Wells
- 👤 Peter Cherish
- 👤 Stephen W. Morgan
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 14:55
CPC Classifications
C; C07; C07C; C07C4/00; C07C4/02; C07C4/04; C10; C10G; C10G9/00; C10G9/14; C10G9/18; C10G9/20
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
182 words
A method of controlling the dilution steam for steam cracking gaseous hydrocarbons which comprises: (a) circulating water upwardly through a tubular saturating zone and heating the water therein at a variably controlled rate by indirect heat exchange with a heating fluid; (b) injecting a gaseous hydrocarbon feed into a lower, flooded portion of the tubular saturating zone in cocurrent flow with the circulating water; (c) recovering a two phase, equilibrium mixture comprised of water and water-saturated hydrocarbon feed from the tubular saturation zone; (d) introducing the two phase, equilibrium mixture to a separation zone having a static liquid pressure greater than that of the tubular saturation zone; (e) recovering a water stream from the separation zone and recirculating the recovered water stream to the tubular saturating zone; (f) recovering a mixed feed vapor stream of gaseous hydrocarbon fully saturated with water from the separation zone; (g) controlling the rate of indirect heat exchange in the tubular saturation zone by selecting a controlling temperature of the mixed feed vapor stream; and (h) introducing the mixed feed vapor stream to a steam cracking zone.
Claim 2
Independent Claim
182 words
A method of controlling the dilution steam for steam cracking gaseous hydrocarbons which comprises: (a) circulating water upwardly through a tubular saturating zone and heating the water therein at a variably controlled rate by indirect heat exchange with a heating fluid; (b) injecting a gaseous hydrocarbon feed into a lower, flooded portion of the tubular saturating zone in cocurrent flow with the circulating water; (c) recovering a two phase, equilibrium mixture comprised of water and water-saturated hydrocarbon feed from the tubular saturation zone; (d) introducing the two phase, equilibrium mixture to a separation zone having a static liquid pressure greater than that of the tubular saturation zone; (e) recovering a water stream from the separation zone and recirculating the recovered water stream to the tubular saturating zone; (f) recovering a mixed feed vapor stream of gaseous hydrocarbon fully saturated with water from the separation zone; (g) controlling the rate of indirect heat exchange in the tubular saturation zone by selecting a controlling temperature of the mixed feed vapor stream; and (h) introducing the mixed feed vapor stream to a steam cracking zone.
Claim 3
Dependent Claim
52 words
The method of claim 1 wherein the heating fluid is steam at a pressure between 0 and 7.2 bar, the pressure of the mixed feed vapor stream is between 2.7 bar and 8.3 bar, and the selected controlling temperature of the mixed feed vapor stream is between 88° C. and 160° C.
Claim 4
Dependent Claim
17 words
The method of claim 1 wherein the water flows through the tubular saturating zone by thermosiphon circulation.
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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) | 1993-07-09 | 1994-01-08 | 1994-07-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-07-09 | 1998-01-08 | 1998-07-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-07-09 | 2002-01-08 | 2002-07-10 | $7700.00 | Window Closed / Lapsed |