US4134732A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Floating methanol plant
Assignee: ConocoPhillips Co
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Filing: 1977-06-08
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Granted: 1979-01-16
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Expires: 1997-06-08
Abstract
Abstract Methanol is produced from offshore natural gas in a plant positioned on a floating structure. The plant incorporates heat recovery equipment and storage facilities providing the flexibility to operate portions of the plant independently so that motion-sensitive parts of the plant, such as tall distillation columns for methanol purification, can be operated only during good weather, while sections of the plant less sensitive to motion can operate during more severe weather.
Inventors
- 👤 Robert G. Jackson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 05:35
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/14; B01D3/143; B01J; B01J19/00; B01J19/0053; B63; B63B; B63B35/00; B63B35/44; C; C02; C02F; C02F1/00; C02F1/02; C02F1/04; C02F1/16; C07; C07C; C07C29/00; C07C29/15; C07C29/151; C07C29/1516; C07C29/1518; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00074; B01J2219/00087; B01J2219/00103; B01J2219/00159; Y; Y02; Y02A; Y02A20/00; Y02A20/124; Y02P; Y02P20/00; Y02P20/50; Y02P70/00; Y02P70/10; Y10; Y10S; Y10S203/00; Y10S203/17; Y10S203/24; Y10S203/25
Claims Analysis
Total Claims: 3
Claim 1
Independent Claim
271 words
In a plant for producing methanol from natural gas, said plant being mounted on a floating structure and comprised of a steam-natural gas reformer, a synthesis reactor and a distillation unit for purification of methanol produced in the synthesis reactor and wherein steam-containing gas from the reformer provides heat for the distillation unit, the improvement comprising: a desalination unit for making fresh water for said plant from sea water, said desalination plant utilizing heat from reformed gas produced in said reformer; fresh water storage means for storing desalinated water produced in said desalination unit, said fresh water storage means having a capacity sufficient to store enough desalinated water to operate said plant for at least three days; heat exchanger means between said reformer and said synthesis reactor for reboiling bottoms from said distillation unit, said heat exchanger means being adapted to exchange heat between said reformed gas and the bottoms from said distillation unit; alternate heat exchanger means between said reformer and said synthesis reactor for conditioning reformed gas ahead of said synthesis reactor, said alternate heat exchanger being cooled by water from the body in which said floating structure is floating and having sufficient capacity to condition reformed gas going to said synthesis reactor when said desalination unit and said distillation unit are not being operated; crude methanol storage means between said synthesis reactor and said distillation unit, said crude methanol storage means having a capacity of at least three days of crude methanol production; and means for selectively shutting down said desalination unit and said distillation unit during adverse weather while said reformer and synthesis reactor continue to operate.
Claim 2
Dependent Claim
271 words
In a plant for producing methanol from natural gas, said plant being mounted on a floating structure and comprised of a steam-natural gas reformer, a synthesis reactor and a distillation unit for purification of methanol produced in the synthesis reactor and wherein steam-containing gas from the reformer provides heat for the distillation unit, the improvement comprising: a desalination unit for making fresh water for said plant from sea water, said desalination plant utilizing heat from reformed gas produced in said reformer; fresh water storage means for storing desalinated water produced in said desalination unit, said fresh water storage means having a capacity sufficient to store enough desalinated water to operate said plant for at least three days; heat exchanger means between said reformer and said synthesis reactor for reboiling bottoms from said distillation unit, said heat exchanger means being adapted to exchange heat between said reformed gas and the bottoms from said distillation unit; alternate heat exchanger means between said reformer and said synthesis reactor for conditioning reformed gas ahead of said synthesis reactor, said alternate heat exchanger being cooled by water from the body in which said floating structure is floating and having sufficient capacity to condition reformed gas going to said synthesis reactor when said desalination unit and said distillation unit are not being operated; crude methanol storage means between said synthesis reactor and said distillation unit, said crude methanol storage means having a capacity of at least three days of crude methanol production; and means for selectively shutting down said desalination unit and said distillation unit during adverse weather while said reformer and synthesis reactor continue to operate.
Claim 3
Dependent Claim
24 words
A plant according to claim 1 including piping means for returning product from the distillation unit directly back to the crude methanol storage means.
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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) | 1982-01-15 | 1982-07-17 | 1983-01-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-01-15 | 1986-07-17 | 1987-01-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-01-15 | 1990-07-17 | 1991-01-16 | $7700.00 | Window Closed / Lapsed |