Refrigeration method and installation

Abstract

Method and installation for refrigerating the same application by means of several refrigerators/liquefiers disposed in parallel, the refrigerators/liquefiers in parallel using a working gas of the same nature having a low molar mass, that is to say having a mean total molar mass of less than 10 g/mol such as pure gaseous helium, each refrigerator/liquefier comprising a station for compressing the working gas, a cold box intended to cool the working gas at the output from the compression station, the working gas cooled by each of the respective cold boxes of the refrigerators/liquefiers being put in thermal exchange with the application with a view to supplying cold to the latter, in which a single compression station compresses the working gas for each of the respective separate cold boxes of the refrigerators/liquefiers disposed in parallel, the single compression station comprising only compression machines of the lubricated-screw type and systems for removing oil from the working fluid output from the compression machines, so that the compression machines and the oil-removal systems are shared by the refrigerators/liquefiers disposed in parallel.

Claims

1. An installation for the cryogenic refrigeration of a same application using several refrigerators/liquefiers, the refrigerators/liquefiers using a working gas having a mean total molar mass of less than 10 g/mol, wherein: each refrigerator/liquefier receives working gas from a single shared compression station so that each of the refrigerators/liquefiers is in downstream flow communication in parallel from the single shared compression station, the single shared compression station compressing the working gas, each refrigerator/liquefier comprising an associated cold box cooling and expanding the working gas at an output from the single shared compression station to a cryogenic temperature; the working gas that is cooled by each of the cold boxes of the refrigerators/liquefiers supplies cold to said same application via thermal exchange; and said single shared compression station comprising two or more compression machines only of the lubricated-screw type and two or more systems for removing oil from the working fluid from the compression machines, so that each of the compression machines and the oil-removal systems is shared by the refrigerators/liquefiers in downstream flow communication in parallel.

2. The installation of claim 1, wherein the two or more compression machines provide the working fluid at several pressure levels.

3. The installation of claim 2, wherein passage of a pressure of the working fluid from one pressure level to a higher pressure level is achieved via one or more of the compression machines in series or in parallel.

4. The installation of claim 2, wherein passage of a pressure of the working fluid from at least one pressure level to a higher pressure level is achieved via two of the compression machines disposed in parallel, the oil-removal system comprising either a single oil-removal member disposed at outlets of the two compression machines disposed in parallel or two oil-removal members each one of which is disposed at a respective outlet of a respective one of to the two compression machines disposed in parallel.

5. The installation of claim 2, further comprising at least one exchanger for cooling the working fluid downstream of at least one of the compression machines.

6. The installation of claim 1, wherein: the two or more compression machines comprise first, second, and third compression machines providing the working fluid at a corresponding three increasing pressure levels above a pressure level of the working fluid at an inlet of the compression station, the first and second compression machines are disposed in series and provide, at respective fluid outlets thereof, the working fluid at respective low and high pressure levels, the third compression machine is supplied at an inlet thereof with working fluid issuing from the cold boxes at a medium pressure level between the low and high levels, the third compression machine providing the working fluid at a fluid outlet thereof at a pressure level equal to the pressure of the working fluid provided at the fluid outlet of the second compression machine.

7. The installation of claim 6, wherein the two or more compression machines further comprise a fourth compression machine disposed in parallel with the second compression machine, an outlet of the fourth compression machine being connected to the inlet of the third compression machine.

8. The installation of claim 6, wherein an outlet of the third compression machine and the outlet of the second compression machine are connected to a common conduit providing the working gas at the same high pressure level.

9. The installation of claim 6, wherein the outlet of the third compression machine and the outlet of the second compression machine are connected to at least one cold box at separate locations providing the working gas at respective separate high pressure levels.

10. A method for refrigerating a same application with a refrigeration and/or liquefaction installation comprising several refrigerators/liquefiers, the refrigerators/liquefiers using a working gas having a mean total molar mass of less than 10 g/mol, wherein: each refrigerator/liquefier receives working gas from a single shared compression station so that each of the refrigerators/liquefiers is in downstream flow communication in parallel from the single shared compression station, the single shared compression station compressing the working gas, each refrigerator/liquefier comprising an associated respective cold box adapted and configured to cool and expand the working gas discharged from the single shared compression station where the working gas is brought to a cryogenic temperature upon discharge from the cold box; the working gas cooled and expanded by the respective cold boxes of the refrigerators/liquefiers supplies cold to said same application via heat exchange; the single shared compression station comprising solely compression machines of the lubricated-screw type and systems for removing oil from the working fluid discharged from the compression machines, so that each of the compression machines and the oil-removal systems is shared by the refrigerators/liquefiers in downstream flow communication in parallel.

11. The method of claim 10, where the working gas comprises helium.

12. The method of claim 10, wherein the working gas essentially consists of helium.

Description

BRIEF DESCRIPTION OF THE FIGURES

(1) The invention may also concern any alternative device or method comprising any combination of the above or following features.

(2) Other particularities and advantages will emerge from a reading of the following description given with reference to the figures, in which:

(3) FIG. 1 shows in a simplified fashion the structure and functioning of an installation according to the invention,

(4) FIG. 2 shows a partial schematic view illustrating the structure and functioning of a first example embodiment according to the invention,

(5) FIG. 3 shows a partial schematic view illustrating the structure and functioning of a second example embodiment according to the invention,

(6) FIG. 4 shows a partial schematic view illustrating the structure and functioning of a third example embodiment according to the invention.

DETAILED DESCRIPTION OF THE INVENTION

(7) The refrigeration installation shown schematically in FIG. 1 comprises several refrigerators/liquefiers (L/R) disposed in parallel, which cool the same physical entity (that is to say the same application 1).

(8) The refrigerators/liquefiers (L/R) disposed in parallel use a working gas of the same nature having a low molar moss, that is to say having a mean total molar mass of less than 10 g/mol such as pure gaseous helium for example.

(9) Each refrigerator/liquefier (L/R) uses a station 2 for compressing the working gas and a cold box 3 intended to cool the working gas output from the compression station 2. The working gas cooled by each of the respective cold boxes 3 of the refrigerators/liquefiers (L, R) is put in heat exchange, via a distribution circuit 11, with the application 1 with a view to supplying cold to the latter.

(10) According to an advantageous particularity, a single compression station 2 compresses the working gas for each of the separate respective cold boxes 3 of the refrigerators/liquefiers L/R disposed in parallel.

(11) The compression 2 station 2 may where applicable be connected to a so-called hot buffer 12 for storing working fluid. According to another advantageous particularity, the single compression station 2 comprises compression machines solely of the lubricated-screw type and systems for removing oil from the working fluid at the discharge from the compression machines. In this way, the compression machines (lubricated-screw compressors) and the oil-removal systems are shared by the refrigerators/liquefiers disposed in parallel.

(12) This configuration makes it possible to limit the number of machines and items of equipment necessary for compressing the working fluid.

(13) This also makes it possible to concentrate the variations in load over a limited number of compressors with suitable regulation means (for example frequency variators, regulator valves, etc.).

(14) In addition, this also where applicable makes it possible to group the compression stations by type of compressor or by function (refrigeration cycle and/or customer supply) rather than by refrigeration cycles.

(15) The architecture also where applicable makes it possible to provide several fluid cycle pressures per function or per compression station.

(16) FIG. 2 illustrates a first possible example embodiment according to the invention. As can be seen in FIG. 2, the single common compression station 2 comprises a plurality of compression machines EC1, EC2, EC3 defining several pressure levels VLP, LP, MP, HP, HP1, HP2 for the working fluid.

(17) At the inlet of the compression station 2, the fluid issuing from one or more cold boxes 3 arrives at a so-called very low pressure (VLP). This very low level pressure depends on the application 1 and this very low pressure level may not be present for some applications (that is to say the first pressure level in the compression station is said to be low, that is to say included in the range mentioned below). A first compression machine EC1 provides a pressure rise in the working fluid to a so-called low pressure LP that is higher than the very low pressure VLP. At the discharge from this first compression machine EC1, the fluid may be de-oiled in an oil-removal member 4 and then cooled in a heat exchanger 5. The discharge of the first compression machine EC1 is then connected to the inlet of a second compression machine EC2, which compresses the fluid from the basic pressure LP to a high pressure HP. The inlet of this second compression machine EC2 also receives the fluid at this low pressure level LP issuing from the cold boxes 3. As before, at the discharge from this second compression machine EC2, the fluid may be de-oiled in an oil-removal member 4 and then cooled in a heat exchanger 5. Before returning to the cold boxes 3, the fluid may undergo a last more selective oil removal in final oil-removal system 14. A third compression machine EC3 is disposed in the compression station 2. This third compression machine EC3 is supplied at its inlet with fluid from the boxes 3 at a so-called medium pressure MP intermediate between the low LP and high HP levels. This third compression machine EC3 also defines at its fluid outlet a high pressure level HP for the working fluid. At the discharge from this second compression machine EC2, the fluid may be de-oiled in an oil-removal member 4 and then cooled in a heat exchanger 5. The high-pressure working fluid is injected upstream of the final oil-removal system 14 (a pipe is connected to the outlet of the second compression machine EC2.

(18) This solution therefore combines several lubricated-screw compression machines between the low pressure LP and high pressure HP and in addition has a compression level between the intermediate pressure MP and the same high pressure HP.

(19) This configuration has the advantage of reducing the size of the primary oil-management systems 4 (oil-removal system 4 before the final oil removal 14) in particular on part of the cycle between the low pressure LP and the high pressure HP. This architecture also makes it possible simultaneously to preserve flexibility on the variations in flow rate and pressure possible in this part of the circuit (in particular between the medium pressure MP and the high pressure HP).

(20) On the other hand this solution is less flexible with regard to the possibility of varying the flow rate of working fluid in the low pressure LP since the combined compression machines are interdependent and the fluctuations are more difficult to control.

(21) Each of the compression stages implemented by a compression machine may of course be replaced by two (or more) compressors disposed in parallel. This is because, depending on the flow rates of working fluid necessary, each compression level may be divided into several compressors disposed in parallel. In this case, the primary oil management (oil removal) and cooling systems may be common to several compressors or be dedicated to each one.

(22) According to the very low pressure level VLP and the compression ratio of the first compression machine EC1, the outlet of the first compression machine EC1 may also be connected to the inlet of the third compression machine EC3 at a so-called medium pressure level MP. The rest of the architecture remaining similar.

(23) The variant in FIG. 3 is distinguished from that in FIG. 1 only in that the installation comprises a fourth compression machine EC12 disposed in parallel with the second compression machine EC2. In the same way as for the second compression machine EC2, the fluid inlet of the fourth compression machine EC12 is connected both to the outlet of the first compression machine EC1 and to a fluid inlet at this low pressure from the cold boxes 3. The outlet of the fourth compression machine EC12 is for its part connected to the inlet of the third compression machine EC3 (the inlet of the third compression EC3 also receives fluid at the medium pressure MP from the cold boxes).

(24) As before, the second EC2 and fourth EC12 compression machines in parallel may each have at their outlet a dedicated oil-removal system 4 and a dedicated heat exchanger 5. In a variant these oil-removal systems 4 and heat exchanger 5 may be common and therefore shared.

(25) As before, according to the working fluid flow rates required, each compression level may be divided into several machines (compressors) disposed in parallel.

(26) As before also, this solution combines several compressors between the low pressure LP and the high pressure HP and in addition provides a compression level between the intermediate pressure MP and the same high pressure HP.

(27) In the case of FIG. 3 however, part of the flow of working fluid at low pressure LP passes through compression machines EC12 that compress the fluid only to the intermediate pressure MP.

(28) The latter compression machines EC12 may be equipped with speed variators in order to react to variations in low-pressure fluid flow rate. The recirculation of fluid between the low pressures LP and medium pressure MP is also possible in order to react to variations in load.

(29) The compressor or compressors EC2 combined between the low pressure LP and the high pressure HP may function with a constant flow rate and independently of the fluctuations in load (application 1) and working cycle. The fluctuations in flow rates and pressures are absorbed by the group of compressors EC1, EC2, EC12 between the very low input pressure VLP as far as the higher levels (LP.fwdarw.MP.fwdarw.HP).

(30) The variant in FIG. 4 is distinguished from that in FIG. 3 only in that the outlets of the third compression machine EC3 and second compression machine EC2 are connected to at least one cold box 3 at separate locations defining respective separate high pressure levels HP1, HP2 for the fluid. In addition, in FIG. 4, the conduit comprising the fourth compression machine EC12 and the downstream members thereof (oil-removal unit 4 and heat exchanger 5) has been shown in broken lines (in order better to show the optional character thereof).

(31) In this configuration of FIG. 4, each high-pressure outlet HP1, HP2 of the third EC3 and second EC2 compression machines comprises, downstream of a respective heat exchanger 5, a respective final oil-removal member 14. Two final oil-removal systems 14 are in fact essential because of the difference in pressure between the two lines.

(32) As before, part of the flow of fluid at low pressure LP is compressed directly to a high pressure HP2. In this configuration in FIG. 4, this high pressure HP2 is independent of the high pressure HP1 obtained at the outlet of the compressors that compress between the medium pressure MP and the high pressure HP1.

(33) This architecture also makes it possible to optimise the sizes and efficiencies of the various types of compressor of the various compression stages.

(34) The variations in flow rate and pressure of the fluid on the circuits resulting respectively in the two high pressure levels HP1 and HP2 can therefore also be managed more independently.

(35) The circuit comprising a compression stage between the medium pressure MP and high pressure HP1 in general supplies the majority of the pressure-reduction turbines of the cycle of the cold boxes 3 that are the refrigeration source of the system. A variation of this cycle therefore permits a direct variation of the refrigeration capacity of the refrigerators/liquefiers L/R.

(36) On the other hand, the high-pressure fluid circuit HP2 issuing from the second compression machine EC2 may be used preferentially for supplying an application 1 and/or an expansion circuit of a cooling of the Joule-Thompson type at the cold end of the cycle.

(37) The invention may in particular apply to any refrigeration/liquefaction unit with a high liquefaction or refrigeration capacity using helium or a rare gas.

(38) By way of non-limitative example (circuit with three compression stages but defining four pressure levels), the respective pressure levels very low VLP, low LP, medium MP and high HP of the compression stages as well as the corresponding compression ratios and flow rates of the working gas may be included in the following ranges.

(39) TABLE-US-00001 aspiration pressure of the flow rates in corresponding the compression compression compression ratios of Compression machine machine the compression stage stage (in bar) (in g/s) (without unit) VLP 0.05 .fwdarw. 1.0 10 .fwdarw. 500 2 .fwdarw. 15 LP 1.0 .fwdarw. 2.5 500 .fwdarw. 2000 2 .fwdarw. 5 HP 3 .fwdarw. 6 800 .fwdarw. 4500 2 .fwdarw. 5

(40) The architectures of the compression stations in the examples illustrated may advantageously, apply also to an installation using a single liquefier/refrigerator (rather than several in parallel).

(41) While the invention has been described in conjunction with specific embodiments thereof, it is evident that many alternatives, modifications, and variations will be apparent to those skilled in the art in light of the foregoing description. Accordingly, it is intended to embrace all such alternatives, modifications, and variations as fall within the spirit and broad scope of the appended claims. The present invention may suitably comprise, consist or consist essentially of the elements disclosed and may be practiced in the absence of an element not disclosed. Furthermore, if there is language referring to order, such as first and second, it should be understood in an exemplary sense and not in a limiting sense. For example, it can be recognized by those skilled in the art that certain steps can be combined into a single step.

(42) The singular forms a, an and the include plural referents, unless the context clearly dictates otherwise.

(43) Comprising in a claim is an open transitional term which means the subsequently identified claim elements are a nonexclusive listing i.e. anything else may be additionally included and remain within the scope of comprising. Comprising is defined herein as necessarily encompassing the more limited transitional terms consisting essentially of and consisting of; comprising may therefore be replaced by consisting essentially of or consisting of and remain within the expressly defined scope of comprising.

(44) Providing in a claim is defined to mean furnishing, supplying, making available, or preparing something. The step may be performed by any actor in the absence of express language in the claim to the contrary.

(45) Optional or optionally means that the subsequently described event or circumstances may or may not occur. The description includes instances where the event or circumstance occurs and instances where it does not occur.

(46) Ranges may be expressed herein as from about one particular value, and/or to about another particular value. When such a range is expressed, it is to be understood that another embodiment is from the one particular value and/or to the other particular value, along with all combinations within said range.

(47) All references identified herein are each hereby incorporated by reference into this application in their entireties, as well as for the specific information for which each is cited.