Gas analyzer with improved architecture for operation in potentially hazardous environment

The invention relates to a gas analyzer with an improved architecture for operation in a potentially hazardous environment .

The European patent EP 3 627 274 Bl discloses a fluid pressure control apparatus for a gas chromatograph which comprises a solenoid valve , that can be actuated through an electronic controller, and pressure sensor . The fluid pressure control apparatus is designed to meet an intrinsic safety standard, for example TEC 60079- 11 . The electronic controller is accommodated in a housing that encloses the valve with its solenoids and the pressure sensor . Portions of a pipe for transporting gases like hydrogen pass through the housing and are connected through fittings .

Moreover, the European patent application EP 3 882 737 Al teaches a gas chromatograph that comprises an explosion-proof housing which connects to a mani fold block, through which a gas , hydrogen e . g . , is transported in a tube . The mani fold block encloses the valve portion of a valve and a pressure sensor . A solenoid portion of the valve is accommodated in the adj acent explosion-proof housing .

WO 2012 / 021681 Al discloses an intrinsically safe thermal conductivity detector for a process gas chromatograph . It comprises a thermistor, a reference resistor connected to the thermistor and an operational ampli fier configured to drive a voltage through the reference resistor onto the thermistor . It further comprises an infallible resistance element connected between the thermistor and a high impedance input of the operational ampli fier . Gas analyzers , in particular gas chromatographs , are used for measuring the component makeup of gases and liquids like that are utili zed in chemical production processes or natural gas coming from a gas well . For detecting di f ferent kinds of components , di f ferent supply and carrier gases are used, including combustible or potentially hazardous gases like hydrogen or other gases such as nitrogen, helium or argon and air . At the same time , there is demand for more ef ficient safety for the operation of gas analyzers . In addition to that , gas analyzers are to be reliable and cost-ef fective . It is an obj ect of the invention to provide a gas analyzer that of fers an improvement in at least one of these aspects .

That obj ect is achieved through a gas analyzer according to the present invention . The gas analyzer comprises a pressure module through which a gas is to be transported . The pressure module at least partly encloses a tube , through which the gas flows during operation of the gas analyzer . The pressure module is sel f-contained . Gas only enters or exits the pressure module only through fittings provided for that purpose . Thus the pressure module may be configured to maintain a gas pressure on its inside that is not af fected by an ambient pressure . The gas transported through the tube may be a carrier gas or another supply gas . Particularly, the gas may be hydrogen or any other gas that can form an explosive mixture with air, or gases like helium, nitrogen, argon or air . Furthermore , the gas analyzer comprises at least one sensor that is accommodated in the pressure module . The at least one sensor is configured to measure a physical quantity inside the pressure module and/or the tube . Moreover, the gas analyzer comprises at least one valve that is configured to control a gas flow through the tube . The valve and the sensor are operable through a master control circuit . The master control circuit is configured to define setpoints , for example for a closed loop control circuit accommodated in the pressure module . This closed loop control circuit may be configured for reading measurement data from the sensor and for actuating the valve respectively . In combination, they are suitable to reliably control the gas flow through the tube depending on the present operational situation of the gas analyzer .

Particularly, the valve and the sensor may be configured to govern a gas flow to a subsequent component of the gas analyzer, e . g . a separation column .

According to the present invention, the master control circuit is accommodated in a sel f-contained control enclosure that is located separate of the pressure module . Thus , the control enclosure separates the master control circuit from the valve and the sensor, which are accommodated in the pressure module . Such a separate accommodation of these components allows economical installation even in potentially hazardous areas .

In turn, potentially hazardous supply gases like hydrogen are separated from the control enclosure in a reliable and cost- ef fective manner .

Additionally, the gas analyzer can use control circuits , especially master control circuits , with more energy-demanding functions , like processing of measurement data or execution of computer programs on the master control circuit . Since the master control circuit is placed in the control enclosure and separated from an atmosphere where hazardous gases may occur and separated from the pressure module , that is purposed to control flow of even flammable supply gases , and no potentially flammable supply gases are conducted into the control enclosure . Furthermore , requirements for cost ef fective measures to operate the gas analyzer can be met . That allows for manufacturing and operating the gas analyzer in a cost- ef fective manner . Altogether, the gas analyzer according to the present invention shows an appropriate safety level , a wider variety of additional data processing functions , and is cost-ef fective to produce and operate . In an embodiment of the claimed gas analyzer, one or more valves are at least partly accommodated in an encapsulation . The encapsulation is configured to engul f at least a portion of the valve where a signi ficant amount of energy is stored . Through the encapsulation, an outer atmosphere that might contain potentially flammable gases is kept from reaching the solenoid portion of the valve .

The encapsulation may be embodied as a casting compound that is an electric insulator, especially a resin, a thermoplastic material or a comparable material . Such an encapsulation is cost-ef fective to manufacture . Moreover, the encapsulation with the at least partly engul fed valve may be accommodated inside the pressure module or outside of it . Alternatively, the valve may be at least partially accommodated in a molding .

Furthermore , the valves may at least partly be placed outside of the pressure module . A placement of the valves as a part of the pressure module outside of the control enclosure decreases heat dissipation from valves within the control enclosure . This allows operation in a broader range of ambient temperature .

In addition to that , the master control circuit of the claimed gas analyzer may comprise at least one intrinsic safety barrier circuit . The intrinsic safety barrier circuit is configured to connect to at the least one sensor and the valve . Particularly, the intrinsic safety barrier circuit serves for supplying limited energy to a closed control circuit , which controls the valve and the at least one sensor . Moreover, the intrinsic safety barrier circuit is configured to facilitate a data trans fer between the master control circuit and the closed loop control circuit , comprising of at least one sensor and/or the at least one valve . That allows for actuating the at least one valve , reading measurement data from the at least one sensor and/or calibrating either of them . The intrinsic safety barrier circuit comprises passive electronic components , especially diodes , Zener diodes and fuses , which are configured to limit the energy supplied to the pressure module to a fixed maximum energy value . A fixed maximum voltage and current limitation is chosen to ensure that intrinsically safety conditions are met . The intrinsic safety barrier circuit allows for supplying a suf ficient amount of energy to the at least one sensor and to the at least one valve . In a preferred embodiment of the invention, the intrinsic safety barrier circuit may be configured according to the IEC 60079- 11 standard . Since the claimed intrinsic safety barrier circuit is at least partly made of passive electronic components , it can be manufactured in a cost-ef fective manner and shows a high degree of reliability .

In another embodiment of the present invention the pressure module in combination with the valve and the at least one sensor is designed in the way that requirements regarding safe operation can be met .

The gas analyzer shows a safety level on par with existing protection standards for gas chromatographs while omitting the use of heavy sophisticated components like metal housings or enclosures for the pressure module .

For example , the pressure module may be designed to withstand operational internal pressures of up to 15 bar . Operational internal pressures of up to 15 bar are commonly not considered to meet the requirements of explosion protection as outlined in various standards . Thus , the pressure module is to be construed as a non-explosion-protected enclosure in comparison to other known gas chromatographs. Therefore , the pressure module may be embodied as a relatively simple , light and cost-ef fective enclosure . Having such an enclosure as the pressure module allows for simpli fying the overall design of the claimed gas analyzer .

Moreover, the at least one sensor in the claimed gas analyzer can be a first pressure sensor . The first pressure sensor is exposed to a gas pressure that is present in the pressure module , especially a gas pressure close to the inlet of the pressure module . This may be used as an entrance pressure read . The gas pressure inside the pressure module is not immediately af fected by an ambient pressure and thus serves as a suf ficiently precise reference pressure . Thus , the first pressure sensor is configured to detect a depleting gas supply . The first pressure sensor may be attached to the tube upstream of the at least one valve . Thus , the first pressure sensor may be configured to measure a pressure in the gas that is supplied to the at least one valve .

Based on the pressure in the gas downstream of the at least one valve and its actuation, the pressure in the gas downstream of the at least one valve it adj usted . The pressure in the gas downstream of the at least one valve to a flow restriction defines the maximum flow of the gas that can be achieved downstream .

The pressure in the gas upstream of the at least one valve may be construed as an inlet mani fold pressure of the tube . For the pressure of the gas upstream of the at least one valve , a simple measurement is suf ficient . Thus , the first sensor may have an increased measuring inaccuracy . Such a simple sensor is cost-ef fective and is still suf ficient to indicate i f there is a suf ficient supply pressure for the gas . That allows for implementing a warning when the supply pressure of the gas falls below a critical threshold or other features recogni zing or predicting failures rooted in the gas supply system .

Furthermore , since information based on internal sensors such as the first pressure sensor is always available , it may be used for operational procedures supporting reliable operation e . g . shut down or startup procedures .

Due to the integration of the first pressure sensor into the pressure module signi ficant ef forts for integration, engi- neering and measures to achieve compatibility for external sensors are avoided . With such a first pressure sensor, the reliable and cost-ef fective operation of the claimed gas analyzer is facilitated .

Alternatively or additionally, the at least one sensor may comprise a temperature sensor . The temperature sensor is accommodated in the pressure module and is configured to measure a temperature there . The measured temperature is used as an input for a compensation function that is a part of a control program that operates the at least one valve . Based on that , the actuation of the at least one valve is adapted to adj ust for thermal ef fects which af fect the at least one sensor, e . g . the first pressure sensor, and/or the at least one valve . Furthermore , the pressure module may comprise of a memory with a calibration data field for at least one of the sensors , especially the second pressure sensor, which allows for such a compensation function . Additionally, pressure variations may be compensated, too . Thus , the gas flow through the at least one valve may be precisely adj usted for a subsequent chromatographic analysis . Furthermore , the claimed gas chromatograph allows for omitting a thermal condition control in the pressure module . As a result , the claimed gas analyzer does not need any temperature stabili zing means and/or pressure stabili zing means which allows for a simple and cost- ef fective design and reliable operation .

Furthermore , the intrinsic safety barrier circuit comprises connectors for at least one , preferably at least four, more preferably at least six, further preferably, at least eight channels . Each channel is utili zed to control a valve that governs the gas flow through a separate tube . That allows for supplying multiple doses of gas as a carrier gas or other supply gases , which may each be used for a parallel chromatographic analysis or complex analytical solutions and combinations . The control functions of multiple channels may be concentrated in a single master control circuit . Among others , the invention is based on the surprising finding that a sin- gle master control circuit may provide suf ficient power for multiple valves and sensors . The more channels the gas chromatograph encompasses , the more complex chromatographic analysis may be performed . The claimed invention allows for increasing the versatility of a gas chromatograph without unduly increasing its dimensions while maintaining an increased safety level .

In another embodiment of the present invention, the intrinsic safety barrier circuit is configured to operate at a temperature of at least 85 ° C . The separation of the master control circuit from the at least one valve and the at least one sensor through the intrinsic safety barrier circuit allows for the use of more robust components for the intrinsic safety barrier circuit . Furthermore , the control program that encompasses the compensation for thermal ef fects on the tube has theoretically no operational limit . Thus , the claimed gas chromatograph can also be operated at increased temperatures . That in turn allows for limiting or even omitting temperature stabili zing means in the claimed gas analyzer .

In yet another embodiment of the claimed gas analyzer, the master control circuit is configured to provide at least 3 . 0 W of power . Preferable the control circuit may be configured to provide at least 6 . 0 W of power . Such power levels provide suf ficient power for multiple valves and sensors in the pressure module or modules which may be operated simultaneously . Therefore , the claimed gas analyzer shows an enhanced degree of versatility and is suitable for further improvements or extensions .

The claimed gas analyzer may also comprise a second pressure sensor as one of the at least one sensor . The second pressure sensor is configured to measure a pressure in the tube which transports the gas . Moreover, the second pressure sensor is located downstream of the at least one valve . Since the second pressure sensor is located downstream of the at least one valve , it is not subj ected to pressure fluctuations in the inlet mani fold pressure . The second pressure sensor is configured to be a part of a closed control loop with the at least one valve .

As the at least one valve is not subj ected to pressure fluctuations in the inlet mani fold, a closed control loop function of the closed control loop may omit any compensating functions for that and is able to obtain an increased precision . Furthermore , the second pressure sensor may be configured to be connected to a calibrated reference as a reference pressure . The reference pressure may be provided by a pressuri zed container . Compared to an ambient gas pressure as a reference pressure like atmosphere pressure , the calibrated reference is robust against fluctuations of ambient air pressure . Such fluctuations may occur when the gas analyzer is accommodated in a shelter, especially one with a purging system . Moreover, such fluctuations may be caused by an ef fluent collection system that is to carry away potential exhaust fluids from the gas analyzer, e . g . processed sample and carrier gas . Using such a calibrated reference pressure stabili zes the operation of the claimed gas analyzer and allows for reliably yielding exact measurements . The claimed gas analyzer of fers an improved level of precision and is robust against unfavorable ambient conditions at the same time .

In another embodiment of the present invention, the second pressure sensor has a higher precision than the first pressure sensor . In that context , a higher precision is to be construed as having a smaller measurement error . The second pressure sensor may be a pressure sensor with a measurement error on the order of l O Oppm, whereas the first pressure sensor may be a pressure sensor with a measurement error of up to 5 percent . Due to that , the first pressure sensor may be embodied as a simple and cost-ef ficient pressure sensor which serves for sensing the inlet mani fold of the pressure module and thus emulating a fixed pressure switch . In turn, the second pressure sensor is substantially insulated from pressure fluctuations in the inlet mani fold and is capable to perform a pressure measurement with an increased precision . Complex compensating means for pressure fluctuations may be omitted in the second pressure sensor . Thus , the present invention utili zes the first and second pressure sensor in more appropriate manners and is also cost-ef fective .

The obj ect outlined above is also achieved by the claimed method for simulating the operational behavior of a gas analyzer . In context with the claimed method, the terms "gas analyzer" and " simulated gas analyzer" may be construed as being interchangeable . The operational behavior may comprise the progression of thermodynamic variables of a gas transported through it , e . g . its temperature , density, pressure , heat energy and/or enthalpy . It may also comprise it combustion behavior, i . e . the ignition behavior of the gas , its burn rate , its volume expansion, its released heat energy and/or enthalpy . The method comprises a first step during which a set of data points is provided . The set of data points mirror the functioning of at least a portion of the gas analyzer that is to be simulated . The data points may mirror the design of the respective portion of the gas analyzer or the entire gas analyzer . Particularly, the set of data points may constitute a so-called digital twin or may be part of a digital twin . The expression digital twin is to be construed in accordance with the document US 2017 /286572 Al . The contents of US 2017 /286572 Al are incorporated into this patent application by reference . The set of data points may be provided by loading them into a memory of a computer on which the claimed method may be performed .

The claimed method also comprises a second step in which at least one operational parameter of the gas analyzer is set . The operational parameter may comprise a condition under which the gas analyzer is operated, e . g . an ambient temperature . Additionally or alternatively, the operational parameter may comprise an information about the analysis process that is to be simulated, e . g . which gas or gasses and in which amounts are to be utili zed, the pressures , temperatures and/or flow rates at which the gas or the gasses are provided, and/or the duration of the operation . The second step may be performed by a user and/or through a data interface .

In addition to that , the claimed method comprises a third step in which a computer program product is executed . That computer program product is configured to emulate the operational behavior of the gas analyzer based on the set of data points provided in the first step . The operational behavior is also emulated based on the at least one operational parameter provided in the second step . The set of data points and the operational parameter may be combined by the computer program product which emulates the operation, i . e . the operational behavior, of the gas analyzer under the circumstances defined in the first and second step . That emulated operation is also to be construed as a simulated operation . That serves for determining at least one performance parameter of the gas analyzer . The performance parameter describes an information about events during the simulated operation which are yielded through the simulated operation of the simulated gas analyzer . For example , the performance parameter may comprise thermodynamic quantities like the temperature , density and/or flow rate of a gas that exits a component of the simulated gas analyzer and/or an information about the composition of a gas mixture inside a component of the simulated gas analyzer . The performance parameter may also comprise an information, i f a gas mixture has ignited during the simulated operation, under which conditions that ignition took place and/or an information about a pressure increase caused by that ignition .

In a fourth step, the at least one performance parameter is output to a user and/or a data interface . The fourth step may utili ze a suitable data connection to an output device readable by the user and/or to a di f ferent computer platform that may be configured to process the at least one performance parameter further . According to the present invention, the gas analyzer simulated through the claimed method is a gas analyzer according to one of the embodiments outlined above . The features of the claimed gas analyzer also apply to the claimed method in a corresponding manner . Thus , the features of the claimed gas analyzer also confer to the claimed method .

The claimed gas analyzer shows an increased level of safety since , among other reasons as well , its master control circuit is separated from it pressure module . Complex combustion calculations which include ignitions through sparks and the like may be omitted . Instead, the claimed method may only take into consideration sel f-ignition conditions for the gas or the mixture of gasses present in the pressure module . Particularly, the third step may be performed without to take into account ignitions by sparks and the like . That in turn allows for a signi ficant simpli fication of the simulation performed based on the claimed method . Therefore , the claimed method allows for an accelerated simulation of the operational behavior of a gas analyzer which may be performed on a relatively simple hardware platform with limited a computing capacity . With the claimed method, intended operations of a physical gas analyzer, that is as least partly mirrored by the set of data points , may be optimi zed faster . Particularly, a more comprehensive set of simulations may be performed in a reduced amount of time . Since the claimed gas analyzer also shows an improved aptitude for its own simulation, it may be operated in an ef ficient manner .

The obj ect described in the present application is also achieved through the claimed computer program product . The claimed computer program product is configured to simulate an operational behavior of a gas analyzer . Consequently, the computer program product may comprise code and/or instruction that make a computer perform the simulation of the operational behavior of the gas analyzer . According to the present invention, the operational behavior is simulated through a method according to one of the embodiments described above . The computer program product may comprise a set of data points that at least partly mirror the gas analyzer that is to be simulated . The computer program product may be a so- called digital twin, as it is described in US 2017 /286572 Al . Furthermore , the computer program product may be stored in a machine-readable medium that is configured to interact with a computer . The claimed computer program product may be embodied as software or in a hardwired form, e . g . a chip, an AS IC or an FPGA, or as a combination of software and a hardwired form . Furthermore , the computer program product may be embodied as a monolithic program that is executed on a single hardware platform . Alternatively, the computer program product may be embodied as a modular software , comprising partial programs that are executed on separate hardware platforms and which interact with each other over a suitable data connection, e . g . an ethernet connection, an internet connection or a mobile data service .

In the following, the present invention will be described in more detail in several figures . The figures are to be construed as mutually complementary . Particularly, identical numerals are to be construed as having the same technical meaning . The features of the embodiments shown in the figures may be combined with each other . Additionally, the features of the embodiments shown in the figures may also be combined with the embodiments outlined above . In particular, the figures show :

FIG 1 a layout of a carrier gas supply unit in a first embodiment of the claimed gas analyzer;

FIG 2 an overall layout of a second embodiment of the claimed gas analyzer .

FIG 1 shows a carrier gas supply unit 50 that is utili zed in a first embodiment of the claimed gas analyzer 10 . The carrier gas supply unit 50 comprises a gas reservoir 14 , that supplies a gas 15 , e . g . hydrogen, that is to be fed to a separation column 12 , that is not shown in detail . The gas 15 from the gas reservoir 14 is fed through pressure regulating means 16 and into a pressure module 20 , which encloses an upstream portion 27 of a pipe 22 . The upstream portion 27 of the pipe 22 is connected to a fitting 36 . The gas 15 in the upstream portion 27 of the pipe 22 is subj ected to an upstream pressure 31 , that is to be construed as an inlet mani fold pressure . The upstream portion 27 of the pipe 22 is connected to a valve 24 which is potted in an encapsulation 23 . The encapsulation 23 may be made of a resin, a thermoplastic material or any other castable material that is fit to provide an exclusion of the gas 15 . The valve 24 comprises a valve portion 28 that constitutes a barrier between the upstream portion 27 of the pipe 22 and a downstream portion 29 of the pipe 22 . That barrier may be actuated, i . e . opened or closed, through a solenoid portion 26 of the valve 24 . The actuation of the solenoid portion 26 and therefore the valve 24 is controlled through a valve circuit 25 that is also potted in the encapsulation 23 . Since the solenoid portion 26 may store a signi ficant amount of energy that is capable of ignition, the encapsulation 23 prevents the gas 15 in the pressure module 20 from getting to the solenoid portion 26 , especially if the gas 15 is hydrogen . Thus , the encapsulation 23 constitutes a protection means against explosions and increases the overall safety of the carrier gas supply unit 50 and the gas analyzer 10 .

The downstream portion 29 of the pipe 22 discharges into the separation column 12 that is not shown in detail in FIG 1 . In the downstream portion 29 of the pipe 22 the gas 15 is subj ected to a downstream pressure 33 that is regulated through the valve 24 and determines the pressure at which the gas 15 flows into the separation column 12 . To that end, the pressure module 20 encompasses two sensors 30 that are embodied as pressure sensors 32 , 34 . A first pressure sensor 32 is connected to the upstream portion 27 of the pipe 22 and is configured to measure the upstream pressure 31 . The first pressure sensor 32 utili zes a gas pressure 39 inside the pressure module 20 as a reference pressure . Based on measurements by the first pressure sensor 32 , the gas analyzer 10 is configured to detect a receding upstream pressure 31 and to indicate that the depleting gas reservoir 14 is to be replaced .

The valve 24 substantially shields the downstream portion 29 of the pipe 22 from fluctuations in the upstream pressure 31 , which is to be construed as the inlet mani fold pressure . During a normal operation of the carrier gas supply unit 50 the valve 24 is actuated to adj ust the downstream pressure 33 to a predefined level . To that end, the downstream portion 29 of the pipe 22 is equipped with the second pressure sensor 34 that is arranged to measure the downstream pressure 33 . The valve 24 , the valve circuit 25 and the second pressure sensor 34 are configured to form a closed control loop that regulates the downstream pressure 33 . Moreover, the second pressure sensor 34 is connected to a calibrated reference pressure 35 . Utili zing such a calibrated reference pressure 35 allows for an even more precise adj ustment of the downstream pressure 33 . Particularly, such a calibrated reference pressure 35 is robust against fluctuations of an ambient pressure . Furthermore , the carrier gas supply unit 50 according to FIG 1 may be combined with a purging system and/or an effluent collection system without compromising the obtainable measurement precision .

The second pressure sensor 34 has a higher precision than the first pressure sensor 32 . Thus , the second pressure sensor 34 is apt to adj ust the downstream pressure 33 at an increased precision . The function of the first pressure sensor 32 does not require such a level of precision and is therefore a relatively simple and cost-ef fective sensor 30 . The first and second pressure sensor 32 , 34 are appropriately chosen for their respective functions .

The valve circuit 25 is connected to a control interface 37 that is configured to establish a connection to a control unit 40 . The control unit 40 encompasses a control enclosure 42 in which a master control circuit 44 is accommodated . The control enclosure 42 is sel f-contained and separate from the pressure module 20 . Substantially any exchange of fluids between the respective inside of the control enclosure 42 and the pressure module 20 is inhibited . The master control circuit 44 is connected to an intrinsic safety barrier circuit 44 that serves as an interface to the control interface 37 of the pressure module 20 . Both power and signals 45 are being trans ferred between the control unit 40 and the pressure module 20 through the intrinsic safety barrier circuit 46 . In particular, that power and these signals 45 allow for actuating to valve 24 and communication with the sensors 30 , which comprise the first and second pressure sensor 32 , 34 . The intrinsic safety barrier circuit 46 comprises multiple electronic components which are configured to limit a voltage supplied to the control interface 37 .

The energy supplied to the control interface 37 is limited to a maximum energy that does not allow for ignition inside the pressure module 20 or valve 24 . Even i f gas 15 , especially hydrogen, leaks into pressure module20 , there will be insufficient energy to cause an ignition . The claimed gas analyzer 10 is apt for using flammable gases like hydrogen as a carrier gas 15 for operation . Furthermore , at least a portion of the gas analyzer 10 shown in FIG 1 is mirrored in a set of data points 62 which belong to a computer program product 60 . The computer program product 60 is a digital twin 65 of at least a portion of the gas analyzer 10 . The computer program product 60 is configured to simulate the operational behavior of the gas analyzer 10 .

FIG 2 shows an overall layout of the second embodiment of the claimed gas analyzer 10 that is a gas chromatograph . The gas chromatograph comprises a carrier gas supply unit 50 which provides a carrier gas 15 for a chromatographic analysis that is to be performed with the gas analyzer 10 . The carrier gas 15 is taken from a gas reservoir 14 and fed through a pressure module 20 that is controlled through a control unit 40 . The gas 15 from the gas container 14 , i . e . the carrier gas 15 , is fed to an inj ector 11 where it is mixed with a chroma- tographic sample 13 , which is to be analyzed in the chromatographic process . The mixture of the chromatographic sample 13 and the carrier gas 15 are supplied to a separation column 12 which splits up the chromatographic sample 13 into its constituents . Since the chromatographic sample 13 travels with the carrier gas 15 , a dedicated volume of the chromatographic sample 13 is determined by the downstream pressure 33 which is regulated in the pressure module 20 . The constituents of the chromatographic sample 13 are being analyzed in a detector 17 which detects at least one physical property of multiple constituents of the chromatographic sample 13 . Signals from the detector 17 are ampli fied in an ampli fier unit 18 and fed to a data processing unit 19 . Based in the amplified signals from the ampli fier unit 18 , the data processing unit 19 can identi fy and quanti fy multiple constituents of the chromatographic sample 13 . The carrier gas supply unit 50 is embodied according to the carrier gas supply unit 50 as shown in FIG 1 .

Furthermore , at least a portion of the gas analyzer 10 shown in FIG 2 is mirrored in a set of data points 62 which belong to a computer program product 60 . The computer program product 60 is a digital twin 65 of at least a portion of the gas analyzer 10 . The computer program product 60 is configured to simulate the operational behavior of the gas analyzer 10 .