US4452621A
Expired / Lapsed
US
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Direct cooling crystallization
Assignee: Mobil Oil AS
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Filing: 1982-09-27
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Granted: 1984-06-05
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Expires: 2002-09-27
Abstract
Abstract A crystallization process is improved by employing direct contact cooling whereby a volatile liquid is vaporized to provide the cooling necessary to effect the crystallization. The effluent vapors of the volatile liquid may be liquified and recycled for reuse by manipulation of temperature and/or pressure. In one embodiment, durene is crystallized from a C 10 + aromatics fraction using liquified n-butane as the coolant.
Inventors
- 👤 Patrick E. Fowles
- 👤 Tsoung Y. Yan
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 06:29
CPC Classifications
B; B01; B01D; B01D9/00; B01D9/0004; B01D9/0009; B01D9/0059
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
214 words
A method for operating a crystallization process at minimum initial capital investment and operating costs which comprises: (a) preselecting crystallization zone pressure and temperature conditions sufficient to provide said minimum capital investment and operating costs for the crystallization of a crystallizable material, (b) selecting a direct contact refrigerant based on said crystallization zone pressure and temperature conditions, said direct contact refrigerant being a volatile liquid having a boiling point, at 760 torr, about 0° to about 60° F. below said crystallization zone temperature and a vapor pressure at said crystallization zone temperature about 50 to about 200 torr above said crystallization zone pressure; (c) introducing a liquid comprising said crystallizable material at a temperature above the crystallization temperature of said material into a crystallization zone maintained under said crystallization zone pressure and temperature conditions, said pressure and temperature conditions effective to cause crystallization of said crystallizable material, (d) introducing into the crystallization zone an effective amount of said volatile liquid at about the temperature maintained in said crystallization zone, whereby said volatile liquid vaporizes in said crystallization zone, and said effective amount being sufficient to remove, upon evaporation of said volatile liquid, sufficient heat from the crystallization zone to cause crystallization of said crystallizable material, and (e) recovering crystallized material from said crystallization zone.
Claim 2
Independent Claim
214 words
A method for operating a crystallization process at minimum initial capital investment and operating costs which comprises: (a) preselecting crystallization zone pressure and temperature conditions sufficient to provide said minimum capital investment and operating costs for the crystallization of a crystallizable material, (b) selecting a direct contact refrigerant based on said crystallization zone pressure and temperature conditions, said direct contact refrigerant being a volatile liquid having a boiling point, at 760 torr, about 0° to about 60° F. below said crystallization zone temperature and a vapor pressure at said crystallization zone temperature about 50 to about 200 torr above said crystallization zone pressure; (c) introducing a liquid comprising said crystallizable material at a temperature above the crystallization temperature of said material into a crystallization zone maintained under said crystallization zone pressure and temperature conditions, said pressure and temperature conditions effective to cause crystallization of said crystallizable material, (d) introducing into the crystallization zone an effective amount of said volatile liquid at about the temperature maintained in said crystallization zone, whereby said volatile liquid vaporizes in said crystallization zone, and said effective amount being sufficient to remove, upon evaporation of said volatile liquid, sufficient heat from the crystallization zone to cause crystallization of said crystallizable material, and (e) recovering crystallized material from said crystallization zone.
Claim 3
Dependent Claim
88 words
A method according to claim 1 including the following additional steps: (f) compressing the evaporated volatile liquid of step (d) under substantially isentropic conditions to a pressure at which the compressed evaporated liquid may be effectively condensed by indirect heat exchange with available cooling means, (g) condensing the evaporated volatile liquid by indirect heat exchange with an available coolant; (h) expanding the condensed volatile liquid under substantially isenthalpic conditions to about the crystallization zone pressure, and (i) passing said condensed liquid to step (d) as the volatile liquid.
Claim 4
Dependent Claim
52 words
A method according to claim 2 wherein the liquid of step (e) is a C 10 + aromatics stream, the crystallizable material is durene, the volatile liquid is n-butane, the crystallization zone pressure is about 1400 to about 1500 torr and the crystallization zone temperature is about 65° to about 75° F.
Claim 5
Dependent Claim
30 words
A method according to claim 3 wherein the pressure of step (f) is about 2300 to about 2600 torr and the condensing temperature is about 90° to about 100° F.
Claim 6
Dependent Claim
14 words
A method according to claim 2 wherein the coolant in step (g) is water.
Claim 7
Dependent Claim
17 words
A method according to claim 5 wherein the condensing temperature is about 55° to about 65° F.
Claim 8
Dependent Claim
14 words
A method according to claim 2 wherein the coolant in step (g) is air.
Claim 9
Dependent Claim
40 words
A method according to claim 1 including the following additional steps: (j) condensing the evaporated volatile liquid of step (d) by indirect heat exchange with a refrigerant, and (k) passing said condensed liquid to step (d) as the volatile liquid.
Claim 10
Dependent Claim
52 words
A method according to claim 8 wherein the liquid of step (c) is a C 10 + aromatics stream, the crystallizable material is durene, the volatile liquid is n-butane, the crystallization zone pressure is about 1400 to about 1500 torr and the crystallization zone temperature is about 65° to about 75° F.
Claim 11
Dependent Claim
30 words
A method according to claim 1 wherein the liquid of step (c) is a C 10 + aromatics fraction, the crystallizable material is durene and the volatile liquid is n-butane.
References Cited (Backward Citations)
US2078992A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-06-05 | 1987-12-05 | 1988-06-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-06-05 | 1991-12-05 | 1992-06-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-06-05 | 1995-12-05 | 1996-06-05 | $7700.00 | Window Closed / Lapsed |