US4378984A
Expired / Lapsed
US
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Distillative freezing process for separating volatile mixtures
Assignee: Individual
•
Filing: 1981-08-25
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Granted: 1983-04-05
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Expires: 2001-08-25
Abstract
Abstract The distillative freezing process disclosed is useful in separating a mixture containing at least two volatile components, denoted respectively as A-component and B-component, by simultaneously vaporizing the two components from the mixture under a sufficiently reduced pressure to simultaneously crystallize B-component. The vapor mixture obtained is brought to a condensed state either by a simple condensation operation or a condensation-desublimation operation without being substantially pressurized. The process may be continued to completely eliminate the liquid phase and bring the mixture into the two phase solid-vapor region. Then, the solid phase is no longer contaminated by the adhering liquid phase and gives a high purity B-component on melting. The process is particularly useful in separating mixtures containing close boiling components, such as styrene-ethyl benzene mixtures, p-xylene-m-xylene mixtures and ethylene-ethane mixtures. The process can therefore be used in producing high purity monomers for the plastic industries and high purity chemicals for other industries.
Inventors
- 👤 Chen-yen Cheng
- 👤 Sing-Wang Cheng
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 18:25
CPC Classifications
B; B01; B01D; B01D7/00; B01D7/02; B01D9/00; B01D9/02; B01D9/04
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
243 words
A crystallization separation process for separating a multicomponent mixture that is at least partly in a liquid state and includes at least two key volatile components, denoted respectively as A-component and B-component, into a B-enriched portion and a B-lean portion through formation of a B-enriched solid mass, wherein the two components form a binary system (a) whose characteristic vapor pressure ratio defined as the ratio of the vapor pressure of A-component to that of B-component both evaluated at the triple point temperature of B-component is in the range of 0.1 to 10 and is less than the ratio of the heat of sublimation to the heat of melting of B-component evaluated at the triple point temperature of B-component, and (b) whose constant pressure phase diagram that includes a three phase (B-enriched solid, liquid and vapor) state has a two phase (B-enriched solid and vapor) region covering a substantial concentration range above the temperature of the three phase state and a two phase (B-enriched solid and liquid) region below the temperature of the three phase state, that comprises a first step of forming a first vapor mixture and a first condensed mass that comprises a mother liquor and a solid phase mass enriched in B-component by concurrently vaporizing the two components from the mixture in a first zone under a first temperature and a first pressure that are respectively lower than the triple point temperature and the triple point pressure of the pure B-component.
Claim 2
Dependent Claim
243 words
A crystallization separation process for separating a multicomponent mixture that is at least partly in a liquid state and includes at least two key volatile components, denoted respectively as A-component and B-component, into a B-enriched portion and a B-lean portion through formation of a B-enriched solid mass, wherein the two components form a binary system (a) whose characteristic vapor pressure ratio defined as the ratio of the vapor pressure of A-component to that of B-component both evaluated at the triple point temperature of B-component is in the range of 0.1 to 10 and is less than the ratio of the heat of sublimation to the heat of melting of B-component evaluated at the triple point temperature of B-component, and (b) whose constant pressure phase diagram that includes a three phase (B-enriched solid, liquid and vapor) state has a two phase (B-enriched solid and vapor) region covering a substantial concentration range above the temperature of the three phase state and a two phase (B-enriched solid and liquid) region below the temperature of the three phase state, that comprises a first step of forming a first vapor mixture and a first condensed mass that comprises a mother liquor and a solid phase mass enriched in B-component by concurrently vaporizing the two components from the mixture in a first zone under a first temperature and a first pressure that are respectively lower than the triple point temperature and the triple point pressure of the pure B-component.
Claim 3
Dependent Claim
43 words
The process of claim 1, wherein B-enriched solid is formed as the two components are vaporized and the heat released in the formation of the B-enriched solid is at least partly removed by the concurrent vaporizations of the two components from the mixture.
Claim 4
Dependent Claim
47 words
The process of claim 2, wherein the said first step is continued until the mother liquor phase is reduced to a small amount to thereby transfer a large fraction of the A-component in the original mixture to the first vapor mixture and thereby form a purified B-solid.
Claim 5
Dependent Claim
68 words
The process of claim 3, that further comprises a third step of melting the purified B-solid in the first zone by pressure isolating the zone and supplying heat thereto to thereby transform a minor amount of the B-solid into vapor and raise the zone pressure to a pressure that is higher than the triple point pressure of the B-component, the melt of the B-solid constituting a purified B-product.
Claim 6
Dependent Claim
59 words
The process of claim 1 which further comprises a second step of transforming the first vapor mixture into a second condensed mass that is at least partly in a liquid state in a second zone by transferring heat therefrom while maintaining the vapor under a second pressure that is also lower than the triple point pressure of the B-component.
Claim 7
Dependent Claim
31 words
The process of claim 5, wherein A-component has a greater volatility than the B-component, whereby the second condensed mass constitutes substantially a liquid output that is relatively enriched with the A-component.
Claim 8
Dependent Claim
47 words
The process of claim 6, wherein the said first step is continued until the mother liquid phase is reduced to a small amount to thereby transfer a large fraction of the A-component in the original mixture to the first vapor mixture and thereby form a purified B-solid.
Claim 9
Dependent Claim
68 words
The process of claim 7, that further comprises a third step of melting the purified B-solid in the first zone by pressure isolating the zone and supplying heat thereto to thereby transform a minor amount of the B-solid into vapor and raise the zone pressure to a pressure that is higher than the triple point pressure of the B-component, the melt of the B-solid constituting a purified B-product.
Claim 10
Dependent Claim
77 words
The process of claim 5, wherein the second condensed mass includes a solid phase that is relatively enriched with respect to B-component and at least a portion of the second condensed mass is melted by transferring heat to the mass while maintaining the mass under an elevated pressure that is higher than the second pressure of the second step by vaporizing a minor fraction of the second condensed mass and providing pressure isolation of the second zone.
Claim 11
Dependent Claim
47 words
The process of claim 9, wherein the said first step is continued until the mother liquor phase is reduced to a small amount to thereby transfer a large fraction of the A-component in the original mixture to the first vapor mixture and thereby form a purified B-solid.
Claim 12
Dependent Claim
68 words
The process of claim 10, that further comprises a third step of melting the purified B-solid in the first zone by pressure isolating the zone and supplying heat thereto to thereby transform a minor amount of the B-solid into vapor and raise the zone pressure to a pressure that is higher than the triple point pressure of the B-component, the melt of the B-solid constituting a purified B-product.
Claim 13
Dependent Claim
135 words
The process of claim 5, wherein the B-component is chosen from the following substances: Aluminum Chloride, Terephthalic Acid, Acetylene, Para-formaldehyde, Carbon Dioxide, Ferric Chloride, Hydrogen Cyanide, Hydrogen Chloride, 2,2-Dimethyl Propane, Hexachlorobenzene, 1,3-Butadiyne, Anthraquinone, Ammonia, t-Butyl Alcohol, Hydrogen, Methane, Carbon Tetrabromide, Anthracene, Carbazole, Cyclobutane, Benzene, 1,2,4,5 Tetrachlorobenzene, t-Butyl Chloride, 1,4 Dioxane, Tetrachloroethylene, Chlorine, Chlorine Dioxide, Dimethyl Terephthalate, Salicylic Acid, Pyrocatechol, Formic Acid, Hydroquinone, 1,2,4,5-Tetramethylbenzene, 4-tert-Butylphenol, Camphene, Benzoic Acid, 2-Naphthol, Pyrogallol, Actic Acid, 1,4 Dichlorobenzene, Phthalic Anhydride, Naphthalene, Formaldehyde, Water, 1,2 Ethanediamine, p-xylene, Iodosilane, Maleic Anhydride, Chloroacetic Acid, Acetamide, Succinimide, Acrylic Acid, Dichloroethane, Diacetamide, Oxygen, Phenol, t-Amyl Alcohol, 1-Naphthol, 4-Bromotoluene, 4-Chlorotoluene, 4-Chloroaniline, Cyclohexanol, Piperidine, Acenaphthene, Tetrachloroethylene, Tiglic Acid, p-Nitrotoluene, Biphenyl, Acetanilide, Ethylene, Silicon Tetrachloride, 2,4 Dichlorophenol, 1,3 Butadiene, Epichlohydrin, Menthol, Silane (SiH 4 ), Titanium Tetrachloride, Hydrogen Peroxide, o-Xylene, Styrene, Acrylnitrile, 1-Butene, m-Xylene, Ethane, Trichlorosilane, Ethyl benzene.
Claim 14
Dependent Claim
47 words
The process of claim 12, wherein the said first step is continued until the mother liquor phase is reduced to a small amount to thereby transfer a large fraction of the A-component in the original mixture to the first vapor mixture and thereby form a purified B-solid.
Claim 15
Dependent Claim
47 words
The process of claim 5, wherein the said first step is continued until the mother liquor phase is reduced to a small amount to thereby transfer a large fraction of the A-component in the original mixture to the first vapor mixture and thereby form a purified B-solid.
Claim 16
Dependent Claim
68 words
The process of claim 14, that further comprises a third step of melting the purified B-solid in the first zone by pressure isolating the zone and supplying heat thereto to thereby transform a minor amount of the B-solid into vapor and raise the zone pressure to a pressure that is higher than the triple point pressure of the B-component, the melt of the B-solid constituting a purified B-product.
Claim 17
Dependent Claim
47 words
The process of claim 1, wherein the said first step is continued until the mother liquor phase is reduced to a small amount to thereby transfer a large fraction of the A-component in the original mixture to the first vapor mixture and thereby form a purified B-solid.
Claim 18
Dependent Claim
68 words
The process of claim 16, that further comprises a third step of melting the purified B-solid in the first zone by pressure isolating the zone and supplying heat thereto to thereby transform a minor amount of the B-solid into vapor and raise the zone pressure to a pressure that is higher than the triple point pressure of the B-component, the melt of the B-solid constituting a purified B-product.
References Cited (Backward Citations)
US1534130A
Cited
US1901486A
Cited
US2715323A
Cited
US2572933A
Cited
US2737784A
Cited
US3042501A
Cited
US2812645A
Cited
US3930800A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-04-04 | 1986-10-04 | 1987-04-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-04-04 | 1990-10-04 | 1991-04-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-04-04 | 1994-10-04 | 1995-04-05 | $7700.00 | Window Closed / Lapsed |