US4086144A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process and apparatus for the separation of float tars in the tar separator of a coking installation
Assignee: Bergwerksverband GmbH
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Filing: 1976-12-01
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Granted: 1978-04-25
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Expires: 1996-12-01
Abstract
Abstract The so-called float tar which floats on the stream of crude tar and ammonia water in the tar separator of a coking installation and which interferes with the clean separation of crude tar and ammonia water is removed by skimming the float tar off the crude tar and ammonia water mixture and subjecting the separated float tar to comminution and homogenization whereupon the homogenized tar product may be processed either separately or together with the bulk of the tar. An installation for use in the process comprises a tar separator in the form of an open top separator vessel, a channelled structure associated with the separator vessel, means provided in the separator vessel for skimming the float tar off the bulk of the crude tar and ammonia water and passing it into the channel of said structure, and a comminuting and homogenizing device which communicates with said channel through a grade drop.
Inventors
- 👤 Heinz Grulich
- 👤 Ernst Otte
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 06:07
CPC Classifications
C; C10; C10C; C10C1/00
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
116 words
A process for the separation of so-called float tar occurring in a tar separator where float tar, crude tar and ammonia-water layers are formed in the mass received for separation from the collector chamber of a coking installation, the said process comprising the steps of skimming the float tar consisting of a mixture of tar, coal dust, water and gas bubbles off the ammonia-water mixture flowing above the crude tar and passing the skimmed float tar to a comminuting and homogenizing zone and homogenizing and comminuting the float tar therein so as to convert it into a high viscosity tar which is then further processed either separately or together with the bulk of the crude tar.
Claim 2
Dependent Claim
116 words
A process for the separation of so-called float tar occurring in a tar separator where float tar, crude tar and ammonia-water layers are formed in the mass received for separation from the collector chamber of a coking installation, the said process comprising the steps of skimming the float tar consisting of a mixture of tar, coal dust, water and gas bubbles off the ammonia-water mixture flowing above the crude tar and passing the skimmed float tar to a comminuting and homogenizing zone and homogenizing and comminuting the float tar therein so as to convert it into a high viscosity tar which is then further processed either separately or together with the bulk of the crude tar.
Claim 3
Dependent Claim
30 words
The process of claim 1 wherein the float tar after separation is passed by gravity drop to the area where it is to be subjected to said comminution and homogenization.
Claim 4
Dependent Claim
39 words
The process of claim 1 wherein any residual flow tar remaining after said skimming action is removed by passing the ammonia water through a dam by which the residual float tar is removed from the flow of ammonia water.
Claim 5
Dependent Claim
166 words
An installation for the separation of float tar occurring in the tar separator of a coking plant where an ammonia water-crude tar mixture is received from a collector chamber of the coking plant, said installation comprising an open-top tar separator for receiving and separating said float tar and said ammonia-water mixture from said crude tar; a channel in said tank separator normally floatingly supported on said ammonia-water mixture and extending across said tank separator; skimming means in the form of a bucket wheel revolving in said tank separator for skimming the float tar from the ammonia-water mixture flowing in the tank separator and for passing the separated float tar into said channel; and a comminution and homogenizing means provided at one end of said channel for receiving and processing said float tar, whereby a high viscosity tar is formed from said float tar by the comminution and homogenizing means which is then passed for further processing separately or together with the bulk of the crude tar.
Claim 6
Dependent Claim
166 words
An installation for the separation of float tar occurring in the tar separator of a coking plant where an ammonia water-crude tar mixture is received from a collector chamber of the coking plant, said installation comprising an open-top tar separator for receiving and separating said float tar and said ammonia-water mixture from said crude tar; a channel in said tank separator normally floatingly supported on said ammonia-water mixture and extending across said tank separator; skimming means in the form of a bucket wheel revolving in said tank separator for skimming the float tar from the ammonia-water mixture flowing in the tank separator and for passing the separated float tar into said channel; and a comminution and homogenizing means provided at one end of said channel for receiving and processing said float tar, whereby a high viscosity tar is formed from said float tar by the comminution and homogenizing means which is then passed for further processing separately or together with the bulk of the crude tar.
Claim 7
Dependent Claim
36 words
The installation of claim 4 wherein said channel extends at an incline from said tank separator to said comminution and homogenizing means, whereby the separated float tar is gravity fed to said communication and homogenizing means.
Claim 8
Dependent Claim
32 words
The installation of claim 4 wherein a dam is provided downstream of said bucket wheel and channel said dam extending across the tar separator in order to remove any residual float tar.
References Cited (Backward Citations)
US2246224A
Cited
US2395901A
Cited
US2825678A
Cited
US2903407A
Cited
US3414480A
Cited
US3607720A
Cited
US3661719A
Cited
US3767536A
Cited
US3841992A
Cited
US3864251A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-04-24 | 1981-10-24 | 1982-04-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-04-24 | 1985-10-24 | 1986-04-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-04-24 | 1989-10-24 | 1990-04-25 | $7700.00 | Window Closed / Lapsed |