Classifications

• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
  • C10B39/00—Cooling or quenching coke
  • C10B39/02—Dry cooling outside the oven
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P20/00—Technologies relating to chemical industry
  • Y02P20/10—Process efficiency
  • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Definitions

• the invention relates to a method for coke drying cooling according to the preamble of the first claim and a device according to the preamble of claims 3 or 4.
• the pre-chamber and cooling chamber are provided with a cylindrical upper part and a conical taper in the lower outlet.
• the pre-chamber and the cooling chamber are to be designed as two statically independent bunkers, which are gas-tightly connected to each other by means of a compensator at the lower end of the pre-chamber outlet and are held by a common or separate scaffold construction.
• the object of the invention is now to propose an improved generic method and a suitable device, which in particular simple measures to compensate for temperature - X -
• the coke particles with a grain size of 1 to 3 mm are expediently separated in a coarse dust separator in which the direction of flow is first reversed from top to bottom in from bottom to top.
• the prechamber and cooling chamber have a round, approximately equal cross-section and are surrounded by a cylindrical outer jacket made of metal, which acts as a common, self-supporting structure is formed and on which an inner lining made of refractory material is suspended or supported.
• the entire construction is supported on the concrete base and has only one expansion possibility upwards, an expansion device, preferably designed as a water cup seal, being arranged at the upper end of the prechamber.
• an expansion device preferably designed as a water cup seal, being arranged at the upper end of the prechamber.
• According to claim 8 are also in the fireproof inner lining of the antechamber and cooling chamber are arranged at certain intervals with expansion joints.
• a gas-tight metallic jacket is provided overall between the inlet opening of the hot coke into the antechamber and the outlet opening of the cold coke at the outlet lock.
• the coke surface in the antechamber during normal operation is formed as a trough as a result of a certain core flow, into which the hot coke falls when the coke bucket is emptied discontinuously.
• a displacer at the coke inlet opening of the prechamber is no need to install a displacer at the coke inlet opening of the prechamber, as is usual with prechambers without a conically narrowed spout.
• the refractory inner lining has only about 30 to 50% of the thickness of the previous outer walls.
• even smaller areas can be quickly replaced in the case of the refractory plates suspended from the metallic outer wall.
• the prechamber and cooling chamber can be arranged in a cylindrical metal jacket which extends in the vertical direction from the concrete foundation to the filling opening of the prechamber and which forms the self-supporting support structure and has cooling openings distributed uniformly over the entire circumference in the region of the prechamber outlet.
• a cylindrical jacket for the pre-chamber and cooling chamber area which is connected in the area of the pre-chamber outlet by a separate support structure.
• claims 4 and 9 are provided in particular, according to which the ceiling of the cooling chamber and thus the cross section of the gas ring channel above the coke slope to the hot gas channel increases and the discharge cross section for the Hot gas at the upper end of the cooling chamber extends over the entire or almost the entire cooling chamber inner diameter. It is also possible to divide the subsequent hot gas channel into several individual channels with their own compensators. This makes it easier to support the ceiling areas because of the smaller span, and smaller and less expensive compensators can be used.
• the construction of the round antechamber and cooling chamber is particularly advantageously designed by the features of claims 12 to 14.
• radiation cooling surfaces can also be arranged in the cooling chamber above the coke pouring cone.
• FIG. 3 shows partly a horizontal section through the cooling chamber in the area of the hot gas exhaust and partly in plan view the ceiling construction of the antechamber and cooling chamber.
• (1) denotes the antechamber with the coke inlet (3) and the coke outlet (4) and (2) the cooling chamber with the coke outlet (5).
• the outer metallic jacket is designated by (6) in the prechamber (1) and by (7) in the cooling chamber (2).
• the support structure (9) which expediently consists of a truss structure.
• the inner lining (8) made of refractory material is fastened in a suitable manner to the outer metallic supporting structures. This inner lining (8) is suspended from the supporting structures (15) and (16) in the area of the ceiling of the antechamber and cooling chamber.
• the refractory lining is supported on the outer, conical metal wall.
• the self-supporting outer support structure the consists of the jackets (6) and (7) and the intermediate support structure (9), is supported on the concrete foundation (13) and has a uniform expansion direction upwards, so that expansion differences between the upper crane travel level and the coke dry cooling device in the area of the coke inlet (3) e.g. B. with the help of a water cup seal, not shown.
• the cooling gas introduced into the cooling chamber (2) is discharged into the coarse dust separator (19) and from there into the upper end via the extraction cross section (10), the compensators (12), the hot runners (11) the waste heat boiler (22) passed.
• the width of the take-off cross-section (10) corresponds approximately to the inner diameter of the cooling chamber. This is followed by a division into two adjacent hot gas channels (11) which are separated from one another by an intermediate wall (23). The span of the ceiling of the hot gas channel (11) is thus considerably reduced and the compensators (12) are smaller and have an approximately square cross section.
• FIG. 2 shows a modified self-supporting structure.
• a common outer cylindrical casing (20) is provided for the antechamber and the cooling chamber (2), which extends from the lower concrete foundation (13) to the upper edge of the antechamber.
• cooling openings (21) are evenly distributed in the area of the pre-chamber outlet.
• FIG. 4 shows the so-called sloping ceiling (24) of the cooling chamber (2) proposed in claim 4, which rises to the deduction section (10). This achieves an approximately uniform speed of the hot cooling gas in the gas ring channel above the coke slope and in particular in the coke bed.
• (17) denotes an additional hot gas discharge from the prechamber and (18) one of the numerous expansion joints arranged in the prechamber and cooling chamber.

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Materials Engineering (AREA)
• Oil, Petroleum & Natural Gas (AREA)
• Organic Chemistry (AREA)
• Coke Industry (AREA)

Applications Claiming Priority (2)

Publications (1)

Family

ID=6395537

Family Applications (1)

Country Status (3)

Families Citing this family (5)

Family Cites Families (6)

• 1989
  • 1989-12-15 DE DE3941453A patent/DE3941453C1/de not_active Expired - Fee Related
• 1990
  • 1990-12-12 EP EP91900205A patent/EP0505396A1/de not_active Ceased
  • 1990-12-12 WO PCT/EP1990/002160 patent/WO1991009094A1/de not_active Application Discontinuation

Non-Patent Citations (1)

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