GB277955A - An improved tar and a process of obtaining the same - Google Patents
An improved tar and a process of obtaining the sameInfo
- Publication number
- GB277955A GB277955A GB23680/27A GB2368027A GB277955A GB 277955 A GB277955 A GB 277955A GB 23680/27 A GB23680/27 A GB 23680/27A GB 2368027 A GB2368027 A GB 2368027A GB 277955 A GB277955 A GB 277955A
- Authority
- GB
- United Kingdom
- Prior art keywords
- drum
- pipe
- retorts
- discharged
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/02—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/006—Combinations of processes provided in groups C10G1/02 - C10G1/08
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Processing Of Solid Wastes (AREA)
- Tunnel Furnaces (AREA)
Abstract
277,955. Urbana Coke Corporation, (Assignees of Parr, S. W., and Layng, T. E.). Sept. 21, 1926, [Convention date]. Retort furnaces; rotary furnaces; charging and discharging; cooling discharged materials. - In carbonizing coal the fuel is fed into a preheating hopper 2 through which pipes 4, traversed by hot waste flue gases from a pipe 5, pass, and is supplied by a screw conveyer 8 rotating in timed relation to a rotary drum 7, to one end of the latter. This drum is enclosed in a heating cham. ber 13 traversed by hot gases entering by a pipe 20 and leaving by the outlet 5, and its angle of inclination may be. varied by a jack 17. The temperature of the drum is maintained constant by a gas burner 21 controlled by a regulating device 23 and a thermo-couple 22 responsive to the temperature in a discharge hopper 19. The speed of rotation of the drum may be automatically controlled from the regulating device 23. The fuel is discharged into a car 24 mounted on a track 25. Each of the metal retorts 26 has at its lower end a hinged perforated plate 33 connected to an operating rod 34. The retorts are enclosed in refractory walls 27 having passages 37 for the entry of gas and passages 38 from which air is admitted by valve-controlled inlets 40, 41 to burn the gas in contact with the retorts. Combustion products escape by a pipe 45 to heat the drum 7. The coke is discharged into a chambed 46 surrounded by air preheating conduits 48 which lead by a pipe 50 to the retort heating chamber. Specification 270,003, [Class 55 (i), Coking &c.], is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US277955XA | 1926-09-21 | 1926-09-21 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB277955A true GB277955A (en) | 1928-07-12 |
Family
ID=21839831
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB23680/27A Expired GB277955A (en) | 1926-09-21 | 1927-09-08 | An improved tar and a process of obtaining the same |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB277955A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104371752A (en) * | 2014-11-13 | 2015-02-25 | 常熟市高压容器制造有限公司 | Peristaltic solid-phase reactor and combined module |
-
1927
- 1927-09-08 GB GB23680/27A patent/GB277955A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104371752A (en) * | 2014-11-13 | 2015-02-25 | 常熟市高压容器制造有限公司 | Peristaltic solid-phase reactor and combined module |
CN104371752B (en) * | 2014-11-13 | 2016-06-08 | 常熟市高压容器制造有限公司 | Creeping motion type solid phase reactor and combined type module |
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