US4349358A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of mixing a gas and a vaporizable liquid
Assignee: Praxair Technology Inc
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Filing: 1981-03-26
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Granted: 1982-09-14
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Expires: 2001-03-26
Abstract
Abstract A method of mixing a gas and a vaporizable liquid to provide a gaseous mixture having a constant composition, regardless of change in rate of flow, except as hereinafter provided, comprising: (a) introducing a mixture comprising a gas and a vaporizable liquid in predetermined proportions into the tube side of a tube and shell heat exchanger at a flow rate sufficient to cause turbulent flow; (b) introducing a heating fluid into the shell side of the heat exchanger at a temperature sufficient to vaporize at least part of the vaporizable liquid whereby the vaporizable liquid separates into a vapor phase and a liquid phase; and (c) delivering the mixture of gas and vapor phase to a use point and recycling the liquid phase to a point at which it will be mixed with gas for introduction into step (a).
Inventors
- 👤 Gregorio Tarancon
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 18:21
CPC Classifications
B; B01; B01F; B01F23/00; B01F23/20; B22; B22C; B22C9/00; B22C9/12; B22C9/123; Y; Y10; Y10T; Y10T137/00; Y10T137/0318; Y10T137/0324; Y10T137/0329; Y10T137/0352
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
134 words
A method of mixing a gas and a vaporizable liquid to provide a gaseous mixture having a constant composition, regardless of change in rate of flow, except as hereinafter provided, comprising: (a) admixing the gas and the vaporizable liquid in predetermined proportions; (b) introducing the mixture of step (a) at a predetermined pressure into the tube side of a tube and a shell heat exchanger at a flow rate sufficient to cause turbulent flow; (c) introducing a heating fluid into the shell side of the heat exchanger at a temperature sufficient to vaporize at least part of the vaporizable liquid, separating the vaporizable liquid into a vapor phase and a liquid phase; and (d) delivering the mixture of gas and vapor phase to a use point and recycling the liquid phase to step (a).
Claim 2
Independent Claim
134 words
A method of mixing a gas and a vaporizable liquid to provide a gaseous mixture having a constant composition, regardless of change in rate of flow, except as hereinafter provided, comprising: (a) admixing the gas and the vaporizable liquid in predetermined proportions; (b) introducing the mixture of step (a) at a predetermined pressure into the tube side of a tube and a shell heat exchanger at a flow rate sufficient to cause turbulent flow; (c) introducing a heating fluid into the shell side of the heat exchanger at a temperature sufficient to vaporize at least part of the vaporizable liquid, separating the vaporizable liquid into a vapor phase and a liquid phase; and (d) delivering the mixture of gas and vapor phase to a use point and recycling the liquid phase to step (a).
Claim 3
Dependent Claim
21 words
The method defined in claim 1 wherein, in step (b), the gas is saturated with the vapor of the vaporizable liquid.
Claim 4
Dependent Claim
28 words
The method defined in claim 1 wherein, in step (b), about 5 to about 10 percent by weight of the liquid amine is converted to the vapor phase.
Claim 5
Dependent Claim
186 words
A process for delivering a gaseous mixture of nitrogen and triethylamine to a use point comprising: (a) mixing nitrogen gas and liquid triethylamine in an aspirator; (b) passing the mixture through the tube side of a heat exchanger wherein the mixture is heated to a predetermined temperature and the liquid amine separates into a vapor phase and a liquid phase, the flow rate being sufficient to cause turbulence; (c) passing the mixture from step (b) into a pressurized zone wherein the liquid amine falls to the bottom of the zone and is recycled to step (a) and the gaseous mixture of nitrogen and amine rises to the top and passes through a demister wherein entrained droplets of liquid amine are removed from the gaseous mixture and returned to the bottom of the zone; (d) passing the gaseous mixture of nitrogen and amine to the use point when the use point is in operation; and (e) when the use point is not in operation, continuously recirculating the gaseous mixture through a heat exchanger whereby the mixture is maintained in the gaseous state and condensation is essentially avoided.
Claim 6
Dependent Claim
186 words
A process for delivering a gaseous mixture of nitrogen and triethylamine to a use point comprising: (a) mixing nitrogen gas and liquid triethylamine in an aspirator; (b) passing the mixture through the tube side of a heat exchanger wherein the mixture is heated to a predetermined temperature and the liquid amine separates into a vapor phase and a liquid phase, the flow rate being sufficient to cause turbulence; (c) passing the mixture from step (b) into a pressurized zone wherein the liquid amine falls to the bottom of the zone and is recycled to step (a) and the gaseous mixture of nitrogen and amine rises to the top and passes through a demister wherein entrained droplets of liquid amine are removed from the gaseous mixture and returned to the bottom of the zone; (d) passing the gaseous mixture of nitrogen and amine to the use point when the use point is in operation; and (e) when the use point is not in operation, continuously recirculating the gaseous mixture through a heat exchanger whereby the mixture is maintained in the gaseous state and condensation is essentially avoided.
Claim 7
Dependent Claim
18 words
The process defined in claim 4 wherein, in step (b), the nitrogen gas is saturated with amine vapor.
Claim 8
Dependent Claim
28 words
The process defined in claim 4 wherein, in step (b), about 5 to about 10 percent by weight of the liquid amine is converted to the vapor phase.
References Cited (Backward Citations)
US1817667A
Cited
US3399511A
Cited
US3590902A
Cited
US3496702A
Cited
US3788825A
Cited
GB1402355A
Cited
US3931684A
Cited
US3880622A
Cited
US4070424A
Cited
US4166799A
Cited
US4276243A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-09-13 | 1986-03-15 | 1986-09-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-09-13 | 1990-03-15 | 1990-09-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-09-13 | 1994-03-15 | 1994-09-14 | $7700.00 | Window Closed / Lapsed |