Plant for the Production of Hydrogen Through Utilization of Heat Energy Obtained From a Gas-Cooled Nuclear Reactor

Abstract

Disclosed is a plant for the production of hydrogen, preferably for the hydrogenating gasification of coal, through utilization of heat energy derived from a gas-cooled, high-temperature nuclear reactor, comprising: The present invention relates to an installation for the production of hydrogen, preferably for the hydrogenating gasification of coal, through utilization of heat energy obtained from a gas-cooled high-temperature nuclear reactor whereby the heat of the reactor is transferred by means of the cooling gas to a series of tubular cracking ovens and subsequently to a series of steam generating devices connected to the cracking ovens. The high-temperature reactor, the tubular cracking ovens and the steam generators are all installed in pods inside one common vessel made of reinforced concrete and recuperative heat exchanging devices are provided for the process gases passing through the tubular cracking oven in the gas circuit. Nuclear power plants with closed gas-turbine circuits are conventionally designed according to the single-container construction method (single unit design) whereby the reactor, the gas turbine, the condenser and the heat exchangers are all installed inside one common pressure vessel made of reinforced concrete. Plants of such design have been shown in German Offenlegungsschriften Nos. 1,764,249 2,062,934 and 2,241,426. These plants have in common that the energy produced in the reactor core is utilized to drive first a gas turbine and subsequently, electric generators. Also, proposals are extant whereby the energy absorbed by the cooling gas in the reactor core is transferred through a heat exchanger to a secondary circuit which is used for supplying the necessary ambient temperature. Such heat exchanger is likewise integrated inside the pressure vessel of reinforced concrete. In German Auslegeschrift No. 1,933,695 the principle has been established by which the heat stored in the cooling medium of a nuclear reactor is transferred in a heat exchanger to a fluid heat-transfer medium -- for example lead -- which, in turn, passes the heat on to a secondary reaction device. Such heat exchangers and reaction devices are placed in a common housing, which is likewise installed, together with the nuclear reactor, inside a common pressure vessel. The state of the art further provides for the use of heat energy absorbed by a rare gas heated by a nuclear reactor for the production of ethylene or synthesis gas by a thermal cracking of hydrocarbons by means of steam. Such a process is described in German Auslegeschrift No. 1,928,093. In the tubular cracking oven disclosed, the process gas entering the oven is first passed through a heat exchanger installed outside the oven, where the gas absorbs heat evergy from a hot medium, such as the reactor's exhaust gases. Where such heat exchangers are designed as recuperative heat exchangers and are installed inside an explosion-proof steel pressure vessel, considerations concerning safety still require that the pressure vessel itself be installed inside the safety structure surrounding the entire plant. The installation of a tubular cracking oven inside the pressure vessel of stressed concrete presents, however, a number of technical and safety problems involving, for instance, the positioning of the connecting tubing between the cracking oven and the recuperative heat exchanger. It is therefore the object of this invention to substantially reduce such problems through an optimal positioning of the elements comprising the recuperative heat exchanging units by providing a plant for the production of hydrogen, preferably for the hydrogenating gasification of coal. This object has been accomplished according to the invention through utilization of heat energy derived from a gas-cooled, high-temperature nuclear reactor, comprising: The foregoing objective is attained through the present invention by installing the recuperative heat exchanging units likewise in cavities inside the concrete pressure vessel directly adjacent to their respective cracking ovens and by connecting these two components through a coaxial gas duct in which the colder gas flows on the shell side, surrounding the structural elements that are exposed to high temperatures. By installing the recuperative heat exchangers inside the concrete pessure vessel according to the invention, it is possible to considerably reduce the length of the tubes connecting the heat exchangers to the tubular cracking ovens and also, make them easy to embed in the concrete vessel. The last feature is for safety reasons an absolute requirement applying to all tube systems that conduct cracking gases inside the containment. The connecting tubes are designed in the form of coaxial gas ducts in which the colder gas flows around the hot cracking gas carried by the interior pipes; as a result, the temperature stress on the liners which line the passageways for the coaxial gas ducts is greatly reduced. Further essential advantages of the design disclosed here are: The working gas, a mixture of methane and steam, which is to be moved into the tubular cracking ovens is first heated to approximately 650.degree. C. in the recuperative heat exchangers by the cracked gas passing out of the tubular cracking ovens with an exhaust temperature of approximately 820.degree. C. During the passage, the cracked gas is cooled down to approximately 520.degree. C. (the temperature values cited depend upon the overall design of the entire plant and must be considered as approximations). The cracked gas exhausts from the concrete pressure vessel at the temperature mentioned. Because rapid closing safety valves are required, they can therefor be installed directly on the concrete pressure vessel, since the functioning of such valves is assured at a temperature of 520.degree. C. It is advantageous to design the tubes connecting the recuperative heat exchangers to a system for the hydrogenating gasification of coal in such a manner that the tubes come out of the concrete pressure vessel at the bottom, thereby substantially shortening the length of the tubing installed inside the pressure vessel (containment) and making the conduits easy to embed in the concrete vessel wall. Furthermore, the accessibility of the concrete pressure vessel either from the top or from the sides will not be reduced. The cold gas mixture is introduced into the recuperative heat exchangers through connecting tubes installed parallel to the ducts in which cracked gas is moved. The tubular cracking ovens together with steam generators and recuperative heat exchangers are suitably installed in pods, symmetrically around the central cavity containing the high-temperature reactor in such a manner that they can be easily removed. A blower is installed underneath each steam generator. Whereas tubular cracking ovens, the steam generators, and the recuperative heat exchangers are removable from above, the relatively light weight blowers are removable from the bottom. Each component can thereby be removed independently. The entire cooling gas circuit (primary circuit) is subdivided into several indentical loops, each comprising in series the same set of components: a tubular cracking oven, a steam generator, a blower and a system of connecting tubes carrying the cooling gas. All loops are connected to each other only via the high-temprature reactor. In addition to the basic components of the primary circuit integrated inside the stressed-concrete pressure vessel and the system comprising the recuperative heat exchangers, the plant furthermore comprises a set of components for the hydrogenating gasification of coal, and also a stream-turbine circuit comprising a plurality of components. Since the invention is concerned merely with the components installed in the interior of the concrete pressure vessel, a detailed description of these conventional external parts can be omitted. The tubular cracking ovens, the steam generators and the recuperative heat exchangers are all installed in the concrete pressure vessel at such a level that they lay parallel to each other. As a result, it is possible to install in straight lines and in horizontal orientation the conduits conveying cooling gas and process gas between the several pods in each loop, and likewise also the tubes connecting the tubular cracking ovens with the reactor cavity. Straight, horizontal ducts afford the shortest connection between components. Thereby a substantial reduction in the build-up of heat in the concrete is attained. The pipes connecting the tubular cracking ovens with the recuperative heat exchangers in each circuit are installed above the support plates from which the tubular cracking ovens are suspended inside each pod. In the upper section of each tubular cracking oven and above the support plates a separate chamber is provided which is tightly sealed off from the remainder cracking oven by a packing medium; the chamber is filled with pure helium gas and held under higher compression than the cooling gas. Any radioactive contamination of this chamber is thereby absolutely prevented, and consequently, the couplings connecting the individual cracking tubes which are installed in this chamber, are accessible for purposes of replacement of the catalyst inside the cracking tubes. The tubes conducting the cooling gas in each loop are advantageously designed as coaxial tubes whereby the colder gas is moving in each instance through the outer duct. The heated cooling gas streaming out of the reactor at the bottom, moves first through the radial hot-gas ducts which are part of a coaxial gas-tube system. It then enters from below into the tubular cracking ovens, thereby flowing around the cracking tubes, and during this process it is cooled down to a moderate temperature. The gas is then transferred underneath the support plates to the interior tubes of the coaxial duct and enters into the steam generators from above. It flows downward on the shell side (around the pipes of the steam generator) where it is further cooled, and subsequently is compressed in the blower systems installed there. The return flow of the cooling gas from the blowers back to the high-temperature reactor takes place through the exterior pipes of the coaxial gas ducts and coaxially also around the components. To accomplish this, annular passages are installed between the liners of the pods and the components. The gas in each loop is first moved from the blower into an annular passage installed between the steam generator and the pod. Moving upwardly, it flows through the outer coaxial duct into the pod provided for the tubular cracking oven. From there, it passes downwardly into an annular passage between the cracking oven and the liner and it then streams through the outer duct of the coaxial system between the pod in which the tubular cracking oven is installed and the high-temperature reactor. It flows into the reactor cavern, where it then streams upwardly through an annular space between the cavity and the high-temperature reactor, and enters the reactor itself from above. The sequentially described path of the gas flow from the individual blowers up to the reactor offers the advantage that all the structural parts exposed to high temperature installed inside the pods are surrounded by streams of relatively cool gas, whereby the problems connected with heat-insulation are substantially reduced. In a preferred embodiment involving a reactor having a thermal output of 2,000 MW, the primary circuit comprises four identical loops, the components of which are installed inside the concrete pressure vessel at a 90.degree. angle relative to each other. The pods in which the four tubular cracking ovens are installed and those in which the four steam generators and the heat exchangers are installed, have been placed in circular patterns having different radii. All pods are sealed off at the top and bottom by pressure- and gas-tight lids. For the purpose of removing any components, the respective lid is taken off, and after the gas .pipes are disconnected, any component can be taken out as a unit, either from above or below, as the case may be. The tubes connecting the steam generators with the steam turbine assembly, and the tubes which connect the recuperative heat exchangers with the components provided for the gasification of coal are preferably installed so as to pass through the lids, whereby the steam-carrying loops pass through the upper lid, while the recuperative set passes through the lower lid. The mixutre of methane and steam fed into the tubular cracking oven passes through a distributor heat installed above the support place holding the tubular cracking oven and is then distributed over the several cracking tubes. The gas passing through the cracking tubes in a downward direction is cracked by the effect of the heat supply and the catalyst. The cracking gas is brought back through a tube having a smaller diameter than that of the cracking tube in which it is coaxially installed. This smaller tube extends downward into a collector chamber at the lower end of the cracking tubes. The gas is collected in this collector chamber and subsequently passes through the interior tube of the coaxial system to the respective recuperative heat exchanger. The ducts connecting the water or steam sources with the steam generators are designed in a similar manner. The water is first distributed over the various pipes in the steam generator through which it flows centrally in a downward direction, and it subsequently passes from below through the helical tubes of the steam generator. The steam generated is accumulated and eventually blown out of the concrete pressure vessel. A secondary system for the disposal of heat is suitably provided inside the concrete pressure vessel. In the conventional manner, it comprises a blower, a check valve, and a cooler. This emergency cooling system operates independently from the primary circuit and secures the disposal of the reactor's residual fission-generated heat in the event of malfunction and during periods of shut-down of the plant. During normal operation of the nuclear reactor, a small amount of the gas entering the reactor is deflected and flows backwardly through this secondary cooling system. The secondary cooling system has an efficiency factor of 4 .times. 50% and is installed in four pods symmetrically aligned in a circle around the reactor cavern between the pods comprising the components of the primary circuit. The entire plant therefore comprises sixteen pods. The four pods comprising the secondary cooling circuit are smaller than the pods provided for the tubular cracking ovens and those provided for the steam generators, but larger than the pods in which the recuperative heat exchangers are installed. Other objects, features and advantages of the invention will become apparent from the following detailed description of preferred embodiments when read together with the attached figures of drawing. A. a thick-walled pressure vessel; B. a high temperature reactor contained in a centrally oriented cavity within the vessel; C. a plurality of process gas cracking reactors contained within the wall of the vessel; D. a number of steam generators corresponding to the number of the gas cracking reactors, the generators being contained in the wall of the vessel; E. a number of recuperative heat exchangers corresponding to the number of gas cracking reactors, each of the heat exchangers being contained in the wall of the vessel and being positioned closely adjacent one of the gas cracking reactors; and F. a coaxial conduit connecting said adjacent heat exchanger and gas cracking reactor pairs. a. a thick-walled pressure vessel; b. a high temperature reactor contained in a centrally oriented cavity within the vessel; c. a plurality of process gas cracking reactors contained within the wall of the vessel; d. a number of steam generators corresponding to the number of the gas cracking reactors, the generators being contained in the wall of the vessel; e. a number of recuperative heat exchangers corresponding to the number of gas cracking reactors, each of the heat exchangers being contained in the wall of the vessel and being positioned closely adjacent one of the gas cracking reactors; and f. a coaxial conduit connecting said adjacent heat exchanger and gas cracking reactor pairs. 1. that no additional separate splinter-proof steel pressure containers are needed; 2. that the dimensions of the safety vessel (containment) in which the pre-stressed concrete tank is conventionally installed, can be reduced in size, since in the new design no additional space is taken up by the recuperative heat exchangers.

Patent Drawings (2 sheets)

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Sheet 2