# US 7,610,951 B2 · Apparatus and process for cooling hot gas > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 7,610,951 B2 - Document ID: US7610951B2 - Status: Granted - Kind: B2 - Application number: 10/566,907 - Filed: 2004-07-27 - Published: 2008-06-26 - Granted: 2009-11-03 - Earliest claimed: 2003-08-06 - Assignees: Shell Oil Company - Inventors: Eckhard Heinrich Erich Otto Friese; Thomas Paul Von Kossak-Glowczewski; Joachim Papendick; Tycho Agien Van Der Plas; Manfred Heinrich Schmitz-Goeb; Edwin Bernardus Wilhelmus Gerardus Voeten - Web page: https://patentgrep.com/patent/US7610951B2 ## CPC - F28F 9/0229: {Double end plates; Single end plates with hollow spaces} - F28D 7/024: {the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration} - F28D 2021/0075: {for syngas or cracked gas cooling systems} - F28F: DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION (water and air traps, air venting F16) - F28D: HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT (fluid heaters having heat generating means and heat transferring means F24H; furnaces F27; details of heat-exchange apparatus of general) ## Abstract Process to cool hot gas by passing the hot gas through a tube having a main tubular part and an upstream tubular part, wherein (i) the exterior of main tubular part is cooled by an evaporating liquid cooling medium flowing freely around said tube, (ii) the upstream tubular part is cooled by passing fresh liquid cooling medium and a defined part of the liquid cooling medium of activity (i) along the exterior of the upstream end of the tube and (iii) wherein the mixture of fresh cooling medium and the defined part of the liquid medium after being used to cool the upstream tubular part is used in activity (i) as cooling medium. ## Claims ### Claim 1 A process to cool hot gas from a partial oxidation reactor that is fluidly connected at its lower end to a horizontal duct, which horizontal duct is fluidly connected to a tube having a main tubular part which is positioned in a vessel and is arranged vertically therein, and an upstream tubular part which is positioned in said horizontal duct and is arranged horizontally therein, said upstream tubular part being sealingly connected to a tube sheet that is also positioned in said horizontal duct and which is arranged vertically therein, said process comprising passing the hot gas through said tube, (i) cooling the exterior of said main tubular part by an evaporating liquid cooling medium flowing freely inside said vessel and around said tube, (ii) cooling the upstream tubular part and said tube sheet by passing a mixture of fresh liquid cooling medium and a defined part of the liquid cooling medium of activity (i) along the exterior of the upstream tubular part and a side of said tube sheet, and (iii) using as cooling medium in activity (i) the mixture of fresh liquid cooling medium and the defined part of the liquid cooling medium after being used to cool the upstream tubular part and tube sheet. ### Claim 2 (depends on 1) The process according to claim 1, wherein the volume ratio of fresh liquid cooling medium and the defined part of the liquid cooling medium as extracted from activity (i) is between 1:4 and 4:1. ### Claim 3 (depends on 2) The process according to claim 2, wherein the upstream tubular part is cooled by passing fresh liquid cooling medium and a defined part of the liquid cooling medium of activity (i) along the exterior of the upstream end of the tube co-current with the gas flowing within the tube. ### Claim 4 (depends on 2) The process of claim 2, wherein the mixture of fresh liquid cooling medium and the defined part of the liquid cooling medium is injected into a compartment surrounding said upstream tubular part. ### Claim 5 (depends on 4) The process of claim 4, wherein in the event the flow of fresh liquid cooling medium is interrupted, the flow of the defined part of the cooling medium is continued to cool the inlet section of said upstream tubular part in said horizontal duct. ### Claim 6 (depends on 3) The process according to claim 3, wherein the hot gas has a temperature of between 1300 and 1500° C. and a temperature of between 240 and 450° C. after being subjected to the process. ### Claim 7 (depends on 6) The process according to claim 6, wherein the hot gas is obtained in a gasification process, comprising the partial oxidation of a gaseous or liquid hydrocarbon feedstock to a mixture comprising mainly hydrogen and carbon monoxide. ### Claim 8 (depends on 1) The process of claim 1, wherein relatively cold cooling medium is supplied to an elevated position in said vessel to establish a natural circulation of the cooling medium. ### Claim 9 (depends on 8) The process of claim 8, wherein both fresh liquid cooling medium and extracted liquid cooling medium are fed to an elevated position in said vessel. ### Claim 10 An apparatus for cooling hot gas from a partial oxidation reactor comprising: (i) a vessel fluidly connected to said partial oxidation reactor by means of a horizontal duct, said vessel and horizontal duct being provided with a cooling medium compartment, an inlet to supply fresh cooling medium and a outlet for discharge of used cooling medium, said vessel and horizontal duct further provided with an inlet for hot gas and an outlet for cooled gas, at least one heat exchange tube fluidly connecting the inlet for hot gas and the outlet for cooled gas positioned in the cooling medium compartment, wherein the downstream end of said heat exchange tube is positioned in said vessel and arranged vertically therein, and wherein the upstream end of said heat exchange tube is positioned in said horizontal duct and is arranged horizontally therein, said upstream tubular part being sealingly attached to a tube sheet that is also positioned in said horizontal duct and is arranged vertically therein, (ii) a means for extracting a volume of the cooling medium from the cooling medium compartment, and wherein (iii) the upstream end of said heat exchange tube in said horizontal duct is provided with a cooling means comprising means to supply a mixture of the extracted liquid cooling medium and part or all of the fresh liquid cooling medium along the exterior of the upstream end of said heat exchange tube and a side of said tube sheet in said horizontal duct. ### Claim 11 (depends on 10) The apparatus according to claim 10, wherein an annular sleeve is positioned around the upstream end of the heat exchange tube and wherein the annular sleeve has an opening to allow the mixture of extracted cooling medium and part or all of the fresh cooling medium to enter the space between the upstream end of the heat exchange tube and the annular sleeve and an outlet opening fluidly connected to the cooling medium compartment. ### Claim 12 (depends on 11) The apparatus according to claim 11, wherein means to supply part of the fresh cooling medium to an elevated position in the vessel is present. ### Claim 13 (depends on 10) The apparatus according to claim 10, wherein said cooling medium compartment is divided into a plurality of cooling medium compartments, including a first compartment from which a volume of cooling medium is extracted, and a second compartment into which the mixture of extracted cooling medium and fresh cooling medium is supplied, said second compartment being positioned in said horizontal duct. ### Claim 14 (depends on 13) The apparatus of claim 13, wherein an injector is present and is positioned in a wall dividing said first cooling medium compartment and said second cooling medium compartment.