# US 9,434,897 B2 · Divided central tube of a combined quenching and scrubbing system for an entrained flow gasification reactor > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 9,434,897 B2 - Document ID: US9434897B2 - Status: Granted - Kind: B2 - Application number: 14/491,041 - Filed: 2014-09-19 - Published: 2015-03-19 - Granted: 2016-09-06 - Earliest claimed: 2013-09-19 - Assignees: Siemens Aktiengesellschaft - Applicants: Siemens Aktiengesellschaft - Inventors: Frank Hannemann; André Herklotz; Horst Hoppe; Tino Just; Manfred Schingnitz; Darek Schmauch - Web page: https://patentgrep.com/patent/US9434897B2 ## CPC - C10K 1/02: Dust removal - C10K 1/08: by washing with liquids; Reviving the used wash liquors (gas washers B01D) - C10K 1/101: {with water only} - C10K: PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE ## Abstract Devices for a three-stage scrubbing system for treatment of hot crude gases and liquid slag by an entrained flow gasification. Crude gas and slag are conducted downward into a water bath in a central tube. The upper part of the central tube consists of a double-threaded tube screen welded in a gas-tight manner, in which water is injected directly as the first scrubbing and cooling stage in the interior thereof. In the water bath, a bubble column is formed, which simultaneously constitutes the second scrubbing and cooling stage. Surface bodies arranged in three layers increase the scrubbing effect. After leaving the bubble column, the crude gas is again sprayed with water in a cavity, wherein one or more nozzle rings are disposed. This forms the third scrubbing stage. The crude gas then leaves the quenching and scrubbing apparatus in steam-saturated form at 200-220° C. and is sent to further treatment. ## Claims ### Claim 1 A crude gas scrubbing system configured and operable for having a high separation level of particles in an entrained flow gasification unit for the reaction of ash-containing fuels with a gasifying agent containing free oxygen to give a crude gas having a high hydrogen content, the system comprising a gasification reactor operable at temperatures of 1200 to 1900° C. and process pressures up to 10 MPa for processing the fuel through the reactor and for converting the fuel to crude gas and liquid slag, a quencher arranged beneath the gasification reactor, a gas and slag outlet from the reactor into the quencher for transferring the crude gas and liquid slag into the quencher, a central tube in the quencher and connected to the gas and slag outlet and the central tube also dips into a water bath at a lower end of the quencher, an upper section of the central tube comprises a tube screen through which cooling water flows, and a lower section of the central tube comprises a smooth tube, in the region of the tube screen an injector injects quenching water into the stream of crude gas and liquid slag, and wherein the tube screen is configured in the shape of an upright bell and comprises windings of a tube that are welded gas tight to one another for preventing passage of crude gas through the tube screen, at the lower end of the central tube the slag is separated out into the water bath and the crude gas rises upward within a bubble column outside the central tube, a crude gas outlet in the pressure casing of the quencher through which the crude gas leaves the quencher, the crude gas is sprayed from above with quenching water through at least one nozzle ring on a route of the crude gas between the water surface and the crude gas outlet. ### Claim 2 (depends on 1) The crude gas scrubbing system as claimed in claim 1, wherein the tube screen is configured as a multi-turn winding of a tube through which cooling water flows. ### Claim 3 (depends on 1) The crude gas scrubbing system as claimed in claim 1, wherein the tube screen has an inside which is plated. ### Claim 4 (depends on 1) The crude gas scrubbing system as claimed in claim 1, further comprising: the tube screen has a cylindrical neck which overlaps the gas and slag outlet, and a first slag drip-off edge formed on an internal diameter of the tube screen at the overlap. ### Claim 5 (depends on 1) The crude gas scrubbing system as claimed in claim 1, wherein the tube screen comprises a transition piece that widens conically starting at a small diameter at the top portion of the transition piece, and a second slag drip-off edge formed on the small diameter portion of the transition piece. ### Claim 6 (depends on 1) The crude gas scrubbing system as claimed in claim 1, further comprising: a nozzle aperture disposed in the tube screen, and configured to accommodate a nozzle, and the nozzle penetrates the tube screen for injecting quenching water into the stream of crude gas and liquid slag. ### Claim 7 (depends on 6) The crude gas scrubbing system as claimed in claim 6, wherein the nozzle aperture is disposed radially outside the slag drip-off edge. ### Claim 8 (depends on 6) The crude gas scrubbing system as claimed in claim 6, further comprising: the nozzle aperture comprises two tube sections and an annular insert in the nozzle aperture, each tube section having connections into two adjacent ones of the windings of the tube screen such that the cooling water of the tube screen flows around the annular insert; and a nozzle secured by a flange connection in the seat of the annular insert. ### Claim 9 (depends on 1) The crude gas scrubbing system as claimed in claim 1, wherein a length ratio of the tube screen above to the smooth tube below is about 1 to 2. ### Claim 10 (depends on 1) The crude gas scrubbing system as claimed in claim 1, wherein the lower end of the central tube is concentrically surrounded by a guide tube, defining an annular space between the central tube and the guide tube. ### Claim 11 (depends on 10) The crude gas system as claimed in claim 10, further comprising: a lower end of the guide tube arranged lower than the lower end of the central tube which leaves a gap between the central tube and the guide tube for slag discharge. ### Claim 12 (depends on 11) The crude gas system as claimed in claim 11, further comprising: an upper end of the guide tube arranged lower than a surface of the water bath in the quencher. ### Claim 13 (depends on 10) The crude gas scrubbing system as claimed in claim 10, wherein a bubble column forms in the annular space between the central tube and the guide tube. ### Claim 14 (depends on 1) The crude gas scrubbing system as claimed in claim 1, further comprising: the central tube has apertures distributed over a circumference of the central tube and close to the lower end of the central tube. ### Claim 15 (depends on 1) The crude gas scrubbing system as claimed in claim 1, further comprising: the central tube has teeth distributed over the circumference of the central tube at the lower end of the central tube. ### Claim 16 (depends on 1) The crude gas scrubbing system as claimed in claim 1, further comprising: a ring connected via connecting elements to an inner wall of the quencher, and the smooth tube is guided to slide through the ring. ### Claim 17 (depends on 13) The crude gas scrubbing system as claimed in claim 13, further comprising: a grid disposed in at least one horizontal plane in the annular gap between the lower central tube and the guide tube. ### Claim 18 (depends on 17) The crude gas scrubbing system as claimed in claim 17, further comprising: the grid is formed of a coarse mesh with relatively wide recesses; metal end plates staggered with respect to others are inserted into the recesses forming a fine mesh grid. ### Claim 19 (depends on 18) The crude gas scrubbing system as claimed in claim 18, further comprising: the grid has angled metal sheets arranged such that they overlap in a crosswise manner. ### Claim 20 (depends on 17) The crude gas scrubbing system as claimed in claim 17, wherein the grid is integrated between the connecting elements. ### Claim 21 (depends on 1) The crude gas scrubbing system as claimed in claim 1, wherein the crude gas outlet is disposed approximately at the level of a divide between the tube screen and the smooth tube. ### Claim 22 (depends on 1) The crude gas scrubbing system as claimed in claim 1, further comprising: a nozzle ring disposed above the crude gas outlet. ### Claim 23 (depends on 1) The crude gas scrubbing system as claimed in claim 1, further comprising nozzles in the nozzle ring, with alternate ones of the nozzles spraying upward followed by nozzles spraying downward. ### Claim 24 (depends on 1) The crude gas scrubbing system as claimed in claim 1, wherein a velocity of the crude gas in the central tube is below 20 m/s. ### Claim 25 (depends on 1) The crude gas scrubbing system as claimed in claim 1, wherein the annular space takes the form of a cavity such that the crude gas in the cavity has a mean flow rate of less than 0.5 m/s. ### Claim 26 (depends on 1) The crude gas scrubbing system as claimed in claim 1, wherein the system is configured such that the crude gas is cooled in the quencher as far as the steam saturation temperature determined by the process pressure.