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US4198273A Expired / Lapsed US ⏱️ 0.0 years remaining

Apparatus for producing petroleum coke calcinate

Assignee: Wintershall AG
•
Filing: 1978-07-12
•
Granted: 1980-04-15
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Expires: 1998-07-12
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Abstract

Abstract Green petroleum coke is indirectly dried, than calcined in a cylindrical rotary kiln and indirectly cooled utilizing a one-way gas flow in the system. Most of the dust in the vapor from the drying step is directly burned in a steam boiler whose off-gases are used to heat the dryer. Any residual dust in the gas is collected in an electro-filter. This dust together with dust which settles out from the dryer and the kiln is collected and added in controlled amounts to the dried coke before calcining. Hydrocarbons expelled during calcining are partially burned off with a stream of secondary air introduced at the coke exit end of the kiln. Most of the remaining hydrocarbons are burned off before they leave the coke inlet end of the kiln. The calcined coke product contains 0.1% by weight of hydrocarbons. The final off-gas from the process has a residual dust content of less than 100 mg/nm 3 .

Inventors

  • 👤 Max Dudek
  • 👤 Otto Tieke

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 03:48
CPC Classifications
C; C10; C10L; C10L9/00; C10L9/08

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 241 words
Apparatus for calcining petroleum coke comprising in combination an indirectly heated rotating green coke dryer having its discharge end connected to the intake chute of a calcining rotary kiln with a one-way valve permitting gas to flow from said dryer to said intake chute and this intake end of the kiln also being connected to a dust depositing chamber and a lean gas discharge line; an electro-filter connected to said dryer with further means connected to a dust collecting receptacle; a vapor conduit lead with blower from said dryer to a steam boiler; a valve regulator between said kiln and said boiler; means for supplying heating gas, primary air and secondary air to said kiln; said dust depositing chamber connected by means of a dust transporting means to a dust collecting receptacle; a secondary air inlet means for said kiln located on the product discharge end over a burner means; a partly water-cooled brick-lined discharge chute connected to said kiln conveying material from said kiln into an indirectly cooled rotating cooler; an exhaust gas line from said cooler connected to an air-operated injector leading back to the burner in said kiln; means for conducting heated cooling water from said cooler to an air cooler and recirculating the same water into the indirect cooler; connecting said boiler by conduit connection with said indirect dryer and by a further conduit to said electro-filter from which a gas exhaust line connects to a smokestack.
Claim 2
Dependent Claim 241 words
Apparatus for calcining petroleum coke comprising in combination an indirectly heated rotating green coke dryer having its discharge end connected to the intake chute of a calcining rotary kiln with a one-way valve permitting gas to flow from said dryer to said intake chute and this intake end of the kiln also being connected to a dust depositing chamber and a lean gas discharge line; an electro-filter connected to said dryer with further means connected to a dust collecting receptacle; a vapor conduit lead with blower from said dryer to a steam boiler; a valve regulator between said kiln and said boiler; means for supplying heating gas, primary air and secondary air to said kiln; said dust depositing chamber connected by means of a dust transporting means to a dust collecting receptacle; a secondary air inlet means for said kiln located on the product discharge end over a burner means; a partly water-cooled brick-lined discharge chute connected to said kiln conveying material from said kiln into an indirectly cooled rotating cooler; an exhaust gas line from said cooler connected to an air-operated injector leading back to the burner in said kiln; means for conducting heated cooling water from said cooler to an air cooler and recirculating the same water into the indirect cooler; connecting said boiler by conduit connection with said indirect dryer and by a further conduit to said electro-filter from which a gas exhaust line connects to a smokestack.
Claim 3
Dependent Claim 52 words
Apparatus as in claim 1, wherein said discharge chute is provided with an upper brick-built portion having a stair configuration, so that calcinate drops onto calcinate, thereby lessening material abrasion wear on said chute, and so that said calcinate is fed to said indirect cooler at the water-cooled portion of said chute.
Claim 4
Dependent Claim 40 words
Apparatus as in claim 1, wherein the calcining kiln within the inlet zone and the calcining zone, is provided with a ridged lining extending over a length of about one third to two thirds of the length of the kiln.

References Cited (Backward Citations)

US2927062A Cited
US3173852A Cited
US3595542A Cited
US3759795A Cited
US3867261A Cited
US4012202A Cited
US3888621A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-04-15 1983-10-15 1984-04-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-04-15 1987-10-15 1988-04-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-04-15 1991-10-15 1992-04-15 $7700.00 Window Closed / Lapsed

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