US3962129A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Impregnation of coke with an organic compound to produce a molecular sieve
Assignee: Bergwerksverband GmbH
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Filing: 1974-02-04
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Granted: 1976-06-08
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Expires: 1994-02-04
Abstract
Abstract Porous coke is impregnated with an organic compound which remains in the pores thereby causing a reduction in the effective size of the same. This results in molecular sieve coke capable of separating different gases, particularly oxygen and nitrogen, and capable of adsorbing smaller gas molecules more rapidly than larger gas molecules. The organic compound has a boiling point of at least 200°C as measured at atmospheric pressure and of no more than 450°C as measured in vacuum.
Inventors
- 👤 Heinrich Munzner
- 👤 Heinrich Heimbach
- 👤 Werner Korbacher
- 👤 Werner Peters
- 👤 Harald Juntgen
- 👤 Karl Knoblauch
- 👤 Dieter Zundorf
- 👤 Hugo Horbel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 23:22
CPC Classifications
C; C01; C01B; C01B13/00; C01B13/02; C01B13/0229; C01B13/0248; C01B13/0259; C01B13/0262; C01B13/0266; B; B01; B01D; B01D53/00; B01D53/02; C01B21/00; C01B21/04; C01B32/00; C01B32/30; C01B32/306; C01B2210/00; C01B2210/0043; C01B2210/0046
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
191 words
A process for the production of a carbon-containing molecular sieve capable of separating different gases, particularly oxygen and nitrogen, and capable of adsorbing smaller gas molecules more rapdily than larger gas molecules, said process consisting of impregnating coke, having pores of a first size with a solution which includes an organic substance and a solvent for said organic substance which volatilizes more readily than said organic substance, said organic substance having a boiling point of at least about 200°C at atmospheric pressure and at most about 450°C at substantially zero pressure being a member of the group consisting of the light and heavy fuel oil fractions and hard paraffins derived from crude oil and petroleum, the fractions derived from coal tar, phenanthrene, anthracene, hexamethylbenzene, methylnaphthalene, diphenyl, dibenzl, acenaphthene, 1,2,3,4-tetrahydronaphthalene, stilbene, diphenylmethane, triphenylmethane, maleic acid anhydride, paraffin oil, kerosene, lubricating oil and pitch distillation residues; and permitting said solvent to undergo evaporation under conditions such that said organic substance remains in said pores thereby causing a reduction of said first size to an effective second size between about 0.2 and about 0.6 millimicrons, said organic substance being left in a non-coked condition.
Claim 2
Dependent Claim
191 words
A process for the production of a carbon-containing molecular sieve capable of separating different gases, particularly oxygen and nitrogen, and capable of adsorbing smaller gas molecules more rapdily than larger gas molecules, said process consisting of impregnating coke, having pores of a first size with a solution which includes an organic substance and a solvent for said organic substance which volatilizes more readily than said organic substance, said organic substance having a boiling point of at least about 200°C at atmospheric pressure and at most about 450°C at substantially zero pressure being a member of the group consisting of the light and heavy fuel oil fractions and hard paraffins derived from crude oil and petroleum, the fractions derived from coal tar, phenanthrene, anthracene, hexamethylbenzene, methylnaphthalene, diphenyl, dibenzl, acenaphthene, 1,2,3,4-tetrahydronaphthalene, stilbene, diphenylmethane, triphenylmethane, maleic acid anhydride, paraffin oil, kerosene, lubricating oil and pitch distillation residues; and permitting said solvent to undergo evaporation under conditions such that said organic substance remains in said pores thereby causing a reduction of said first size to an effective second size between about 0.2 and about 0.6 millimicrons, said organic substance being left in a non-coked condition.
Claim 3
Dependent Claim
26 words
A process as defined in claim 1, wherein said organic substance has a boiling point of substantially 360°C at most as measured at substantially zero pressure.
Claim 4
Dependent Claim
22 words
A process as defined in claim 1, wherein the impregnating step is carried out at a temperature in excess of room temperature.
Claim 5
Dependent Claim
12 words
A process as defined in claim 1, wherein said coke is particulate.
Claim 6
Dependent Claim
20 words
A process as defined in claim 4, wherein the coke particles have a size between substantially 2 and 10 millimeters.
Claim 7
Dependent Claim
23 words
A process as defined in claim 1, wherein the impregnating step is carried out for a period of substantially 10 to 60 minutes.
Claim 8
Dependent Claim
35 words
A process as defined in claim 1, wherein said organic substance is a member of the group consisting of fuel oil, diphenyl, paraffin, anthracene oil, phenanthrene, paraffin oil, pitch, lubricating oil and maleic acid anhydride.
Claim 9
Dependent Claim
32 words
A process as defined in claim 1, wherein said solvent comprises at least one member of the group consisting of petroleum ether, ethylene chloride, methylene chloride, carbon tetrachloride, acetone, benzene and cyclohexane.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-06-08 | 1979-12-08 | 1980-06-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-06-08 | 1983-12-08 | 1984-06-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-06-08 | 1987-12-08 | 1988-06-08 | $7700.00 | Window Closed / Lapsed |