# US 10,502,368 B2 · Indirect fluid heater > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 10,502,368 B2 - Document ID: US10502368B2 - Status: Granted - Kind: B2 - Application number: 14/914,536 - Filed: 2014-08-29 - Published: 2016-07-21 - Granted: 2019-12-10 - Earliest claimed: 2013-08-29 - Assignees: Intelliheat Solutions Ltd. - Applicants: Intelliheat Solutions Ltd. - Inventors: Stefan Martin Romocki - Web page: https://patentgrep.com/patent/US10502368B2 ## CPC - F17D 1/02: for gases or vapours - F02C 1/02: the working fluid being an unheated pressurised gas - F16L 53/32: using hot fluids - F17D 1/05: Preventing freezing (by heating F16L53/30) - F28D 1/0213: {for heating or cooling a liquid in a tank} - F28D 15/0266: {with separate evaporating and condensing chambers connected by at least one conduit; Loop-type heat pipes; with multiple or common evaporating or condensing chambers (F28D15/043 takes precedence)} - F28D 2021/0064: {Vaporizers, e.g. evaporators} - F17D: PIPE-LINE SYSTEMS; PIPE-LINES (pumps or compressors F04; fluid dynamics F15D; valves or the like F16K; pipes, laying pipes, supports, joints, branches, repairing, work on the entire line, accessories F16L; steam traps or the like F16T; fluid-pressure electric cables H01B9/06) - F02C: GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS (construction of turbines F01D; jet-propulsion plants F02K; construction of compressors or fans F04; generating combustion products of high pressure or high velocity F23R; using gas turbines in compression refrigeration plants F25B11/00) - F16L: PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL - 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 The present invention relates to a heater suitable for heating a flow of natural gas. There is provided a heater (1) suitable for heating a flow of natural gas, comprising a vessel (2) containing a heat transfer fluid, a heat source tube (3) passing through the vessel and being at least partially immersed in the heat transfer fluid, the heat source tube (3) being suppliable with heated gas to allow the heated gas to flow along the heat source tube (3) to evaporate the heat transfer fluid and at least one heat exchanger being connectable to a source of second fluid (9) to be heated, the heat exchanger being arranged so that the second fluid can be heated by the evaporated heat transfer fluid. ## Claims ### Claim 1 A heater for heating a flow of a first gas, comprising: a vessel containing a heat transfer fluid; a heat source tube passing through the vessel and being at least partially immersed in the heat transfer fluid, the heat source tube being suppliable with a heated second gas, the heat source tube being configured to allow the heated second gas to flow along and inside the heat source tube to evaporate the heat transfer fluid; at least one heat exchanger being connectable to a source of the first gas, the at least one heat exchanger being arranged so that the first gas can be heated by the evaporated heat transfer fluid; and at least one of a fan, pump or blower configured to force the heated second gas along the heat source tube, wherein the at least one heat exchanger comprises at least one heat transfer tube being connectable to the source of the first gas so that the at least one heat transfer tube is configured such that an entirety of the first gas received from the source of the first gas is directed to flow inside the at least one heat transfer tube and through the at least one heat exchanger, the at least one heat transfer tube being arranged to be heated by the evaporated heat transfer fluid, the heater further comprising a burner to supply the heated second gas to the heat source tube, and a control system for controlling a vessel pressure in the vessel and a fluid temperature of the heat transfer fluid and for controlling at least one of the burner or the at least one of a fan, pump, or blower, the control system configured to control a circulation rate of the heated second gas in the heat source tube using the at least one of a fan, pump, or blower, the control system configured to operate the vessel with the fluid temperature in a range of 40° C. to 90° C. and with the vessel pressure in an absolute pressure range of 50 mbar to 340 mbar, the control system comprising a digital controller incorporating a thermo-controller, wherein the vessel is an evaporator vessel, the at least one heat exchanger further comprising a condenser vessel in fluid communication with the evaporator vessel via a piping circuit to allow the heat transfer fluid to flow between the evaporator vessel and the condenser vessel in the piping circuit, the at least one heat transfer tube passing through the condenser vessel of the at least one heat exchanger, the evaporator vessel, the condenser vessel, and the at least one heat transfer tube together comprising a sealed fluid system operating under vacuum with the vessel pressure in the absolute pressure range of 50 mbar to 340 mbar, the sealed fluid system employing a fixed mass of the heat transfer fluid held under vacuum in the absolute pressure range of 50 mbar to 340 mbar. ### Claim 2 (depends on 1) The heater according to claim 1, wherein the center of gravity of the condenser vessel is above the center of gravity of the evaporator vessel in an operating condition of the heater. ### Claim 3 (depends on 1) The heater according to claim 1, wherein the heat transfer fluid comprises water and/or propylene glycol or ethylene glycol. ### Claim 4 (depends on 1) The heater according to claim 1, wherein the heat source tube includes at least two straight sections and at least one curved section, the heat source tube defining a sinuous path, the heat source tube tapered along a length of the heat source tube residing within the evaporator vessel in a direction from an inlet to an outlet of the heat source tube, the tapering of the heat source tube decreasing a surface area of the heat source tube thereby promoting compactness of the heat source tube. ### Claim 5 (depends on 1) The heater according to claim 1, wherein the heat source tube has a cone-shaped inlet where the heat source tube enters the evaporator vessel from the burner and an outlet where the heat source tube leaves the evaporator vessel, and the heat source tube is tapered along a length of the heat source tube residing within the evaporator vessel in a direction from the inlet to the outlet. ### Claim 6 (depends on 1) The heater according to claim 1, wherein a single heat source tube passes through the evaporator vessel. ### Claim 7 (depends on 1) The heater according to claim 1, wherein at least a portion of the heat source tube follows a substantially horizontal path inside the vessel in an operating condition of the heater. ### Claim 8 (depends on 1) The heater according to claim 1, wherein the control system is configured to control the at least one of the fan, pump or blower. ### Claim 9 (depends on 1) The heater according to claim 1, wherein the control system is configured to control the burner based on achieving a required temperature of the heat transfer fluid and/or the first gas. ### Claim 10 (depends on 9) The heater according to claim 9, wherein both the heat transfer fluid and the first gas have a corresponding required temperature, the required temperature of the heat transfer fluid being above the required temperature of the first gas. ### Claim 11 (depends on 9) The heater according to claim 9, wherein the control system is configured to control the burner based on achieving a required temperature of the first gas. ### Claim 12 (depends on 1) The heater according to claim 1, wherein one or more temperature sensors are provided to measure a temperature of the first gas after it has passed through the heat transfer tube, or after it has passed through the heat transfer tube and undergone pressure let-down or to measure the temperature of the heat transfer fluid in the evaporator vessel or condenser vessel, and wherein the control system is configured to control at least one of the burner or the at least one of the fan, pump or blower based on an output of one or more of the temperature sensors. ### Claim 13 (depends on 1) The heater according to claim 1, the heater further comprising an isolation vessel connected to the evaporator vessel, the isolation vessel being configured to receive and isolate heat transfer fluid from the evaporator vessel, the heater comprising one or more sensors configured to measure pressure inside the evaporator vessel, wherein the one or more sensors are provided on the isolation vessel. ### Claim 14 (depends on 1) The heater according to claim 1, wherein the condenser vessel is separate from the evaporator vessel. ### Claim 15 A heater for heating a flow of a first gas, comprising: a vessel containing a heat transfer fluid; a heat source tube passing through the vessel and being at least partially immersed in the heat transfer fluid, the heat source tube being suppliable with a heated second gas, the heat source tube configured to allow the heated second gas to flow along and inside the heat source tube to evaporate the heat transfer fluid; and at least one heat exchanger connectable to a source of the first gas, the at least one heat exchanger arranged so that the first gas can be heated by the evaporated heat transfer fluid, wherein the at least one heat exchanger comprises at least one heat transfer tube connectable to the source of the first gas so that the first gas is directed to flow inside the at least one heat transfer tube, the at least one heat transfer tube being arranged to be heated by the evaporated heat transfer fluid, wherein the heater further comprises a burner to supply the heated second gas to the heat source tube, and a control system for controlling a vessel pressure of the vessel and a fluid temperature of the heat transfer fluid, the control system configured to operate the vessel with the fluid temperature in a range of 40° C. to 90° C. and with the vessel pressure in an absolute pressure range of 50 mbar to 340 mbar, the control system comprising a digital controller incorporating a thermo-controller, wherein the vessel is an evaporator vessel, the at least one heat exchanger further comprising a condenser vessel in fluid communication with the evaporator vessel via a piping circuit to allow the heat transfer fluid to flow between the evaporator vessel and the condenser vessel in the piping circuit, the at least one heat transfer tube passing through the condenser vessel of the at least one heat exchanger, the evaporator vessel, the condenser vessel, and the at least one heat transfer tube together comprising a sealed fluid system operating under vacuum with the vessel pressure in the absolute pressure range of 50 mbar to 340 mbar, the sealed fluid system employing a fixed mass of the heat transfer fluid held under vacuum in the absolute pressure range of 50 mbar to 340 mbar, wherein the heat source tube has an inlet where the heat source tube enters the evaporator vessel from the burner and an outlet where the heat source tube leaves the evaporator vessel, and the heat source tube is tapered along a length of the heat source tube located within the evaporator vessel in a direction from the inlet to the outlet, the heat source tube including at least two straight sections and at least one curved section, the heat source tube defining a sinuous path, the tapering of the heat source tube decreasing a surface area of the heat source tube thereby promoting compactness of the heat source tube. ### Claim 16 A heater for heating a flow of a first fluid, comprising: a vessel containing a heat transfer fluid; a heat source tube passing through the vessel and being at least partially immersed in the heat transfer fluid, the heat source tube being suppliable with a heated gas, the heat source tube configured to allow the heated gas to flow along and inside the heat source tube to evaporate the heat transfer fluid; and at least one heat exchanger connectable to a source of the first fluid, the at least one heat exchanger arranged so that the first fluid can be heated by the evaporated heat transfer fluid, wherein the at least one heat exchanger comprises at least one heat transfer tube connectable to the source of the first fluid so that the at least one heat transfer tube is configured such that an entirety of the first fluid received from the source of the first fluid is directed to flow inside the at least one heat transfer tube and through the at least one heat exchanger, the at least one heat transfer tube arranged to be heated by the evaporated heat transfer fluid, wherein the heater further comprises a burner to supply the heated gas to the heat source tube, and a control system for controlling a vessel pressure in the vessel and a fluid temperature of the heat transfer fluid, the control system configured to operate the vessel with a vessel temperature in a range of 40° C. to 90° C. and with the vessel pressure in an absolute pressure range of 50 mbar to 340 mbar, the control system comprising a digital controller incorporating a thermo-controller, wherein the vessel is an evaporator vessel, the at least one heat exchanger further comprising a condenser vessel in fluid communication with the evaporator vessel via a piping circuit to allow the heat transfer fluid to flow between the evaporator vessel and the condenser vessel in the piping circuit, and the at least one heat transfer tube passing through the condenser vessel of the at least one heat exchanger, the evaporator vessel, the condenser vessel, and the at least one heat transfer tube together comprising a sealed fluid system operating under vacuum with the vessel pressure in the absolute pressure range of 50 mbar to 340 mbar, the sealed fluid system employing a fixed mass of the heat transfer fluid held under vacuum in the absolute pressure range of 50 mbar to 340 mbar, wherein one or more temperature sensors are provided to measure a temperature of the first fluid after it has passed through the heat transfer tube, or after it has passed through the heat transfer tube and undergone pressure let-down or to measure the temperature of the heat transfer fluid in the vessel or condenser vessel, and wherein the control system is further configured to control a circulation rate of the heated gas based on an output of one or more of the temperature sensors. ### Claim 17 (depends on 16) The heater according to claim 16, further comprising at least one of a fan, pump, or blower configured to force the heated gas along the heat source tube, the control system configured to control the at least one of the fan, pump, or blower to adjust the circulation rate of the heated gas.