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US4123349A Expired / Lapsed US ⏱️ 0.0 years remaining

Separation of solids containing residues from liquid fractions of a coal hydrogenation process using an expansion engine and a pressure release means

Assignee: Saarbergwerke AG
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Filing: 1977-06-01
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Granted: 1978-10-31
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Expires: 1997-06-01
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Abstract

Abstract A process for the separation of solids containing residues from a liquid fraction containing higher boiling fractions produced in a coal hydrogenation process at elevated temperatures and pressures. The separation process involves two expansion steps, one step in an expansion engine and a subsequent expansion-evaporation step in a pressure release means and a separator chamber, whereby the higher boiling fraction is evaporated and separated from the residue fraction. The separation process in the chamber can be facilitated by creating vacuum conditions therein, or by introducing a foreign gas, preferably heat exchange with the removed hot residue fraction, to thereby reduce the partial pressure of the evaporated higher boiling fraction. The foreign gases can be steam or/and gases obtained from the hydrogenation of the coal.

Inventors

  • 👤 Helmut Wurfel

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 10:51
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/045; C10G1/06

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 109 words
In a process for separation of distillation oils from a liquid product fraction comprising solids containing residues resulting from a hydrogenation process for coal at elevated pressures and temperatures, and from which said product fraction the lower boiling components of said product fraction are separated by expansion and subsequent separation of the phases, the improvement comprising expanding said liquid product fraction in at least two successive steps, a first expansion step effected in an expansion engine in liquid phase wherein no evaporation of said distillation oils occurs, and a second expansion-evaporation step effected in a pressure release means, whereby solids containing residues are separated from said vaporized distillation oils.
Claim 2
Dependent Claim 109 words
In a process for separation of distillation oils from a liquid product fraction comprising solids containing residues resulting from a hydrogenation process for coal at elevated pressures and temperatures, and from which said product fraction the lower boiling components of said product fraction are separated by expansion and subsequent separation of the phases, the improvement comprising expanding said liquid product fraction in at least two successive steps, a first expansion step effected in an expansion engine in liquid phase wherein no evaporation of said distillation oils occurs, and a second expansion-evaporation step effected in a pressure release means, whereby solids containing residues are separated from said vaporized distillation oils.
Claim 3
Dependent Claim 32 words
The process of claim 1, wherein the work energy produced in said expansion step in said expansion engine is used in the form of pumping energy for said hydrogenation process for coal.
Claim 4
Dependent Claim 14 words
The process of claim 1, wherein said expansion-evaporation step is conducted under vacuum conditions.
Claim 5
Dependent Claim 27 words
The process of claim 1, wherein said expansion-evaporation step is conducted in a chamber containing foreign gases, whereby the partial pressure of said distillation oils is reduced.
Claim 6
Dependent Claim 18 words
The process of claim 4, wherein said foreign gases comprise gaseous components from said hydrogenation process for coal.
Claim 7
Dependent Claim 11 words
The process of claim 4, wherein steam comprises said foreign gas.
Claim 8
Dependent Claim 23 words
The process of claim 4, wherein said foreign gas is introduced directly into the expanded vapor-liquid mixture exiting from said pressure release means.
Claim 9
Dependent Claim 27 words
The process of claim 4, wherein said foreign gas is preheated in a heat exchanger with the said solids containing residues removed from said second expansion step.

References Cited (Backward Citations)

GB280734A Cited
US3844928A Cited
US4019975A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-10-30 1982-05-01 1982-10-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-10-30 1986-05-01 1986-10-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-10-30 1990-05-01 1990-10-31 $7700.00 Window Closed / Lapsed

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