CN110873777A - A pilot test device for evaluating low carbon hydrocarbon oxidation catalyst performance - Google Patents
A pilot test device for evaluating low carbon hydrocarbon oxidation catalyst performance Download PDFInfo
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- G01N31/10—Investigating or analysing non-biological materials by the use of the chemical methods specified in the subgroup; Apparatus specially adapted for such methods using catalysis
Abstract
The invention provides a pilot test device for evaluating the performance of a low-carbon hydrocarbon oxidation catalyst, which comprises a raw material preparation system, a reaction system, an absorption system, a lean cycle gas component regulation and control system, a cycle compression system and an online analysis system; the raw material configuration system, the reaction system, the absorption system, the lean circulating gas component regulation and control system and the circulating compression system are sequentially connected and combined into a closed loop; the test device can well solve the problem that the prior pilot test device for the performance of the low-carbon hydrocarbon oxidation catalyst in the gas circulation type process can not effectively adjust the accumulated CO in the circulating gas while ensuring the stable process conditions such as the pressure flow of the device and the likexThe problem of carbon oxide realizes accurate and stable evaluation of the catalyst, and provides important guarantee for catalyst samples from small tests to industrialization.
Description
Technical Field
The invention belongs to the technical field of catalyst research and development processes, and particularly relates to a pilot test device for evaluating the performance of a low-carbon hydrocarbon oxidation catalyst.
Background
The catalytic oxidation process of the low carbon hydrocarbon has important economic value. For example, ethylene oxide prepared by epoxidation of ethylene is applied to raw materials of ethylene glycol for producing chemical fibers, acrolein and acrylic acid prepared by oxidation of propane or propylene are applied to pesticides and coatings, and methacrylic acid prepared by oxidation of isobutene can be applied to production of organic glass. Other novel methods and novel processes for preparing high value-added chemicals by catalytic oxidation of some low-carbon hydrocarbons are also research hotspots of people. In all cases, the technical core of the production process is the low-carbon hydrocarbon oxidation catalyst.
The development of low carbon hydrocarbon oxidation catalysts generally requires three stages of pilot plant research, pilot plant scale-up and industrial testing. The important research content of the pilot scale is to adopt a pilot scale device to evaluate the performance of the amplified catalyst, which is not only the verification of the magnitude amplification of the results of the pilot scale research, but also provides data for a process package under the condition of being closer to the actual production, and reduces the risk of industrial test failure. Therefore, the pilot scale research is a key link in the development period of the low-carbon hydrocarbon oxidation catalyst. Many small-scale catalyst technologies have good reaction results, but cannot be converted into productivity, and various problems often occur in the process of pilot scale-up, wherein one problem is the lack of a proper pilot scale evaluation device.
Although the low-carbon hydrocarbon oxidation catalyst has higher selectivity to the target product, a part of low-carbon hydrocarbon is inevitably deeply oxidized into COxCarbon oxides (by-products) are accumulated along with the reaction cycle if the by-products are not treated in time, because most of the industrial devices for oxidizing the low-carbon hydrocarbons adopt a circulation process. The existing industrial device generally adopts a decarburization separation unit to control the content of carbon oxides in the circulating gas. However, the pilot plant is unrealistic due to the limitation of investment, raw material source and production place, and the matched decarburization separation unit is unrealistic, so if the pilot plant also adopts a circulation process for obtaining the catalyst performance evaluation result closer to the industrial operation condition, how to effectively control the content of carbon oxide while ensuring the accuracy and stability of the evaluation data of the plant becomes a key pointSexual and technical difficulties.
Chinese patent document CN205426877U provides a device for evaluating a primary catalyst, which returns a part of the gas after reaction to the device and discharges some gas, but this proposal does not disclose how to accurately measure the composition of the recycle gas after discharging a part of the gas, and therefore, it is impossible to realize effective control of the content of carbon oxides while accurately stabilizing the evaluation data of the device.
Disclosure of Invention
In order to overcome the defects in the prior art, the invention aims to provide a pilot test device for evaluating the performance of a low-carbon hydrocarbon oxidation catalyst, which can be used for accurately and stably evaluating the catalyst and provides important guarantee for the catalyst sample from pilot test to industrialization.
In the present invention, the lower hydrocarbon refers to hydrocarbon substances with less than 5 carbon atoms in a single molecule, and includes methane, ethane, ethylene, propane, propylene, n-butane, isobutane, 1-butene, 2-butene, isobutene, butadiene, etc.
The purpose of the invention is realized by the following technical scheme:
a pilot test device for evaluating the performance of a low-carbon hydrocarbon oxidation catalyst comprises a raw material preparation system, a reaction system, an absorption system, a lean cycle gas component regulation and control system, a cycle compression system and an online analysis system;
the raw material configuration system, the reaction system, the absorption system, the lean circulating gas component regulation and control system and the circulating compression system are sequentially connected and combined into a closed loop;
the on-line analysis system is connected with at least two systems of the raw material configuration system, the reaction system, the absorption system, the lean cycle gas component regulation and control system and the cycle compression system.
According to the invention, the raw material preparation system is used for preparing the raw material mixed gas according to the content requirements of the raw material components in the process conditions;
wherein the reaction system is used for realizing the catalytic reaction of the catalyst sample;
wherein the absorption system is used for absorbing the target product generated by the reaction system;
wherein the lean cycle gas component regulation and control system is used for regulating and controlling the content of carbon oxide components in the lean cycle gas;
wherein the cyclic compression system is used for returning the lean cycle gas to the raw material configuration system;
wherein the online analysis system is used for online analyzing the component content of the circulating gas so as to regulate the composition of the circulating gas and obtain catalyst reaction data.
According to the invention, the raw material configuration system comprises a mixer for configuring raw materials, the mixer comprises at least three interfaces, namely a first interface, a second interface and a third interface, the first interface is respectively connected with a raw material gas pipeline and a circulating compression system, the second interface is connected with an oxidant pipeline, and the third interface is connected with a reaction system.
According to the invention, the reaction system comprises a reactor, wherein the reactor comprises a reaction tube, a heater, a heat exchange medium container, a first temperature measuring element and a pressure detecting element;
wherein the reaction tube is arranged in a heat exchange medium container; the heat exchange medium container is filled with a heat exchange medium; the first temperature measuring element is used for monitoring the temperature of the heat exchange medium in the heat exchange medium container so as to ensure that the heat exchange medium can reach the required temperature; the pressure detection element is used for monitoring the pressure in the heat exchange medium container and preventing overpressure from damaging the container structure; the heater is used for providing heat for the heat exchange medium.
According to the invention, the reaction tube further comprises a member capable of rapid pressure relief. Optionally, the component is a combination of one or more of a pressure controller, a safety valve and a rupture disc.
According to the present invention, the member capable of rapid pressure release is provided at the upper end and/or the lower end of the reaction tube, for example, the member is provided at the upper end of the reaction tube.
According to the invention, the reaction system further comprises a second temperature measuring element; the second temperature measuring element is used for measuring the temperature of the reaction tube and can be arranged at any one or more positions of the outer side, the inner side and the like of the reaction tube. Exemplarily, the second temperature measuring element is one and is arranged at the inner side of the reaction tube;
or the second temperature measuring element comprises two temperature measuring elements, wherein one temperature measuring element is arranged on the inner side of the reaction tube, and the other temperature measuring element is arranged on the outer side of the reaction tube;
or the second temperature measuring element comprises three temperature measuring elements, wherein one temperature measuring element is arranged on the inner side of the reaction tube, the second temperature measuring element is arranged on the outer side of the reaction tube, and the third temperature measuring element is arranged on the surface of the heater; such an arrangement allows for better testing of the temperature required during the reaction.
According to the invention, the absorption system comprises one or more absorption devices to ensure complete absorption of the product components in the reacted gas. When the absorption device is a plurality of absorption devices, the absorption devices can be arranged in series or in parallel, and the absorption devices are preferably arranged in series.
According to the present invention, the absorption system further comprises a buffer tank located at a lower portion of the absorption apparatus and connected to the absorption apparatus for diluting the absorbent for discharge.
According to the invention, the lean cycle gas component regulation and control system comprises a pressure vessel, one or more automatic discharge component regulation and control pipelines connected with the pressure vessel, one or more automatic discharge pressure regulation and control pipelines connected with the pressure vessel, and a pressure detection element arranged on the pressure vessel;
each automatic discharge component regulation and control pipeline is controlled by an instrument control system respectively, and the gas discharge amount is adjusted in real time according to the component analysis result fed back by online analysis;
each automatic discharge pressure regulation and control pipeline regulates the amount of discharged gas in real time according to the container pressure value fed back by the pressure detection element;
through setting up automatic component regulation and control pipeline of releasing and automatic pressure regulation and control pipeline of releasing, can make poor circulation gas component regulation and control system can also guarantee the stability of test device pressure when satisfying poor circulation gas component regulation and control.
According to the invention, the number of the pressure vessels is one or more; if the number of the pressure vessels is multiple, at least one of the pressure vessels is connected with one or more automatic discharge component regulating and controlling pipelines, at least one of the pressure vessels is connected with one or more automatic discharge pressure regulating and controlling pipelines, and at least one of the pressure vessels is provided with a pressure detection element.
Illustratively, the lean cycle gas component regulating and controlling system comprises a pressure vessel, an automatic discharge component regulating and controlling pipeline connected with the pressure vessel, an automatic discharge pressure regulating and controlling pipeline and a pressure detecting element arranged on the pressure vessel.
Illustratively, the lean cycle gas component regulating and controlling system comprises two pressure vessels, an automatic discharge component regulating and controlling pipeline connected with one of the pressure vessels, an automatic discharge pressure regulating and controlling pipeline connected with one of the pressure vessels or with the other of the pressure vessels, and a pressure detecting element arranged on one of the pressure vessels.
According to the invention, the lean cycle gas after the components are regulated and controlled by the lean cycle gas component regulation and control system is provided with power by the cycle compression system and is circulated back to the raw material preparation system.
According to the invention, the cyclic compression system comprises at least one compressor and a buffer container, the compressor is connected with the lean cycle gas component regulation and control system, and the buffer container is connected with the raw material preparation system through the compressor.
Illustratively, the compressor is connected with a pressure vessel in the lean recycle gas component regulation system, and the lean recycle gas treated by the lean recycle gas component regulation system enters the buffer vessel through the compressor.
According to the invention, the buffer container is also provided with a bypass, the bypass is directly connected with at least one pressure container of the lean circulating gas component regulation and control system, and the buffer container is provided with a pressure detection element.
According to the invention, the on-line analysis system is connected with at least two systems of the raw material configuration system, the reaction system, the absorption system, the lean cycle gas component regulation and control system and the cycle compression system.
Illustratively, the on-line analysis system is connected with at least two of the raw material configuration system, the reaction system and the lean recycle gas component regulation system.
Illustratively, the online analysis system is coupled to the feedstock distribution system and the reaction system.
According to the invention, the on-line analysis system comprises a sampling pipeline, an analysis instrument and a signal transmission line; the sampling pipeline is connected with an analytical instrument; the analysis instrument is connected with an instrument which needs to take the component analysis value as a control basis through a signal transmission line.
The invention has the beneficial effects that:
the invention provides a pilot test device for evaluating the performance of a low-carbon hydrocarbon oxidation catalyst, which can well solve the problem that the existing pilot test device for evaluating the performance of the low-carbon hydrocarbon oxidation catalyst in a gas circulation type process cannot effectively adjust the accumulated CO in the circulating gas while ensuring the stable process conditions such as pressure and flow of the devicexThe problem of carbon oxide realizes accurate and stable evaluation of the catalyst, and provides important guarantee for catalyst samples from small tests to industrialization.
Drawings
Fig. 1 is a schematic view of a catalyst evaluation apparatus of the present invention.
FIG. 2 is a schematic view of a catalyst evaluation apparatus in example 1 of the present invention.
FIG. 3 is a schematic view of a catalyst evaluating apparatus in example 2 of the present invention.
Reference numerals:
in fig. 1, a is a raw material configuration system, B is a reaction system, C is an absorption system, D is a lean cycle gas component regulation and control system, E is a cycle compression system, F is an online analysis system, a solid line is a main process flow, and a dotted line is an analysis sampling pipeline;
in fig. 2, 101 is a first interface; 102 is a second interface; 103 is a third interface; 104 is a mixer; 105 is a mass flow controller; 106 is a reaction tube; 107 is a catalyst; 108 is an electric heater; 109 is a thermocouple for detecting the temperature in the reaction tube; 110 is a thermocouple for detecting the temperature of the heat exchange medium desalted water; 111 is heat exchange medium desalted water; 112 is a pressure sensor for monitoring the pressure in the heat exchange medium container; 113 is a rupture disk; 114 is a packed absorption tower; 115 is a pressure vessel configured for the circulating gas component regulating system D; 116 is a pressure sensor; 117 is an automatic relief pressure regulating and controlling pipeline; 118 is an automatic bleed component regulation and control line; 119 is a diaphragm compressor; 120 is a buffer tank; 121 is a bypass for connecting the pressure container and the buffer tank; 122 is a pressure sensor; 123 is a sampling pipeline; 124 is sample pretreatment equipment; 125 is a mass spectrometer with a multi-channel switching valve.
In fig. 3, 201 is a first interface; 202 is a second interface; 203 is a third interface; 204 is a mixer; 205 is a rotor flow controller; 206. 207, 208 and 209 correspond to reaction tubes having an inner diameter of 31.3mm, 39mm, 45mm and 1in the reaction system B, respectively; 210 is a catalyst sample; 211 is a jacket; 212 is a thermocouple for detecting the temperature in the reaction tube; 213 is a thermocouple for detecting the temperature in the jacket; 214 is heat transfer oil of a heat exchange medium; 215 is a rupture disk; 216 is a plate-type absorption tower; 217 is a first pressure vessel configured for a recycle gas component regulation system D; 218 a second pressure vessel configured for a recycle gas component conditioning system D; 219 is an automatic discharge component regulating and controlling pipeline; 220 is an automatic relief pressure regulating and controlling pipeline; 221 is a pressure sensor; 222 is a diaphragm compressor; 223 is a buffer tank after the compressor; 224 is a bypass with an automatic control instrument for connecting a second pressure vessel configured by the circulating gas component regulating system D with the buffer tank; 225 is a pressure sensor; 226 is a sampling line; 227 is sample pretreatment equipment; 228 is an on-line gas chromatograph with a multi-channel switching valve.
Detailed Description
As described above, the invention provides a pilot test device for evaluating the performance of a low-carbon hydrocarbon oxidation catalyst, which comprises a raw material preparation system a, a reaction system B, an absorption system C, a lean cycle gas component regulation and control system D, a cycle compression system E and an online analysis system F;
the raw material configuration system A, the reaction system B, the absorption system C, the lean circulating gas component regulation and control system D and the circulating compression system E are sequentially connected and combined into a closed loop;
the on-line analysis system F is connected with at least two systems of the raw material configuration system A, the reaction system B, the absorption system C, the lean cycle gas component regulation and control system D and the cycle compression system E.
The raw material preparation system A is used for preparing raw material mixed gas according to the content requirements of the raw material components in the process conditions;
the reaction system B is used for realizing the catalytic reaction of the catalyst sample;
the absorption system C is used for absorbing the target product generated by the reaction system B;
the lean cycle gas component regulation and control system D is used for regulating and controlling the content of carbon oxide components in the lean cycle gas;
the circulation compression system E is used for returning the lean circulation gas to the raw material configuration system A;
the on-line analysis system F is used for analyzing the component content of the circulating gas on line so as to adjust and control the composition of the circulating gas and obtain catalyst reaction data.
In one embodiment, the raw material preparation system a, the reaction system B, the absorption system C, the lean recycle gas component regulation and control system D, and the recycle compression system E are connected in sequence and combined into a closed loop; the meaning is that the raw material configuration system A is connected with the reaction system B, the reaction system B is connected with the absorption system C, the absorption system C is connected with the poor cycle gas component regulation and control system D, the poor cycle gas component regulation and control system D is connected with the cycle compression system E, and the cycle compression system E is connected with the raw material configuration system A.
[ Material preparation System A ]
In a preferred embodiment of the present invention, the raw material configuration system a includes a mixer for configuring the raw material, the mixer includes at least three interfaces, i.e., a first interface, a second interface, and a third interface, the first interface is respectively connected to the raw material gas pipeline and the cyclic compression system E, the second interface is connected to the oxidant pipeline, and the third interface is connected to the reaction system B.
Wherein, the first interface is used for conveying raw material gas (the raw material gas comprises hydrocarbon raw material and inert components), and is also used for recycling gas (namely, circulating gas component) which does not participate in the reaction after the reaction is finished;
the second interface is used for conveying an oxidant; mixing the raw material gas and the oxidant in a mixer;
the third interface is used for conveying the mixed raw material gas and the oxidant to the reaction system B, i.e. can also be understood as an outlet of the mixer.
Illustratively, the feed gas conduit comprises a hydrocarbon feed conduit and an inert component conduit.
In one embodiment, the feed gas pipeline and the oxidant pipeline can be respectively provided with a pressure stabilizing instrument and a flow instrument; all raw materials and the oxidant enter the mixer under the control of a pressure stabilizing and flow instrument. The pressure stabilizing instrument can adopt any type of pressure stabilizing detection instrument as long as the pressure stabilizing detection instrument and the valve can form a feedback control loop; the flow meter may be any type of flow meter as long as it can form a feedback control loop with the valve, wherein preferably, a mass flow controller is used, and more preferably, a thermal mass flow controller is used.
Wherein, besides the raw material gas and the oxidant, the mixer is also mixed with the circulating gas components, the content of the circulating gas components can be regulated and controlled by setting proper flow rate according to the analysis result by an operator, or the component content can be directly used as a feedback value for flow control regulation to automatically regulate, namely, a so-called cascade control method is adopted.
[ reaction System B ]
In a preferred embodiment of the present invention, the reaction system B comprises a reactor, the reactor comprises a reaction tube, a heater, a heat exchange medium container, a first temperature measuring element, and a pressure detecting element;
wherein the reaction tube is arranged in a heat exchange medium container; the heat exchange medium container is filled with a heat exchange medium; the first temperature measuring element is used for monitoring the temperature of the heat exchange medium in the heat exchange medium container so as to ensure that the heat exchange medium can reach the required temperature; the pressure detection element is used for monitoring the pressure in the heat exchange medium container and preventing overpressure from damaging the container structure; the heater is used for providing heat for the heat exchange medium.
The number of the reactors is not particularly limited, and may be adjusted reasonably according to the amount of the reaction raw material, for example, the number of the reactors may be one or more, and if there are more, a plurality of reactors may be arranged in parallel; the reactors can be respectively provided with reaction tubes, heaters, heat exchange medium containers, temperature measuring elements and pressure detecting elements; or a plurality of shared heaters, heat exchange medium containers, temperature measuring elements and pressure detecting elements in a plurality of reactors; the concrete can be adjusted according to the actual situation.
The number of the reaction tubes in each reactor is not particularly limited, and may be appropriately adjusted according to the amount of the reaction raw material, for example, the number of the reaction tubes may be one or more, and in the case of a plurality of reaction tubes, the plurality of reaction tubes may be arranged in parallel, and the heat exchange medium is filled between the reaction tubes.
Wherein, the pressure detecting element can be one or more of a pressure gauge, a pressure transmitter and a pressure sensor.
Wherein a catalyst is accumulated in the reaction tube for catalyzing reaction.
The material of the reaction tube is selected from metal materials with good heat conductivity, and the inner diameter of the reaction tube/the equivalent diameter of the catalyst sample is more than or equal to 3.
The catalyst sample equivalent diameter refers to: and (2) screening the catalyst sample by using two layers of screens with different pore sizes, wherein the screen with larger relative pores is arranged above the screen with smaller relative pores, the shape of each pore is square, when the selected upper layer screen enables the catalyst sample with the mass accounting for 80% of the catalyst sample to pass through, and the lower layer screen enables the catalyst sample with the mass accounting for 80% of the catalyst sample falling through the upper layer screen not to pass through, the average edge length value of each pore of the two layers of screens is divided by 2 to obtain the equivalent diameter of the catalyst sample.
Wherein, the reaction tube also comprises a component capable of rapidly relieving pressure, and the component can be one or more of a pressure controller, a safety valve and a rupture disk. The member is provided at the upper end and/or the lower end of the reaction tube, and more preferably, the member is provided at the upper end of the reaction tube.
Wherein the heater is selected from the group consisting of electric heater, steam heater, microwave heater, infrared heater, etc., as long as the reaction temperature required for the catalyst can be satisfied. Among them, an electric heater is preferable.
Wherein the heat exchange medium is selected from water, heat transfer oil, molten salt, metal bath and the like, as long as the heat exchange requirement for stabilizing the reaction temperature of the catalyst can be met.
The heat exchange medium container needs to meet certain mechanical strength so as to ensure that the structure of the container cannot be damaged when the catalyst reaches the reaction temperature.
The first temperature measuring element is used for monitoring the temperature of the heat exchange medium in the heat exchange medium container and can be arranged at any one or more positions of the heat exchange medium, the surface of the heater and the like. Illustratively, the first temperature measuring element is one and is arranged in the heat exchange medium; or the first temperature measuring element comprises two temperature measuring elements, one temperature measuring element is arranged in the heat exchange medium, and the other temperature measuring element is arranged on the surface of the heater, so that the temperature measuring elements can better ensure that the heat exchange medium can reach the required temperature.
In one embodiment, the reaction system B further comprises a second temperature sensing element; the second temperature measuring element is used for measuring the temperature of the reaction tube.
For example, the second temperature measuring element can be arranged at any one or more positions of the outer side, the inner side and the like of the reaction tube.
Exemplarily, the second temperature measuring element is one and is arranged at the inner side of the reaction tube;
or the second temperature measuring element comprises two temperature measuring elements, wherein one temperature measuring element is arranged on the inner side of the reaction tube, and the other temperature measuring element is arranged on the outer side of the reaction tube;
or the second temperature measuring element comprises three temperature measuring elements, wherein one temperature measuring element is arranged on the inner side of the reaction tube, the second temperature measuring element is arranged on the outer side of the reaction tube, and the third temperature measuring element is arranged on the surface of the heater; such an arrangement allows for better testing of the temperature required during the reaction.
Wherein, each reactor in the reaction system B is provided with at least one temperature measuring element capable of measuring the temperature of the outer side of the wall of the reaction tube.
Wherein, each reactor in the reaction system B is provided with at least one temperature measuring element capable of measuring the temperature of the inner side of the wall of the reaction tube.
Wherein at least one temperature measuring element is capable of measuring the temperature of the heater surface in each reactor in the reaction system B.
[ absorption System C ]
In a preferred embodiment of the present invention, the absorption system C comprises one or more absorption devices to ensure complete absorption of the product components in the reacted gas. When the absorption device is a plurality of absorption devices, the absorption devices can be arranged in series or in parallel, and the absorption devices are preferably arranged in series.
Wherein the absorption equipment may be at least one of a packed column, a plate column, an absorption tank, and the like.
Wherein the absorption equipment contains an absorbent for absorbing the product components, and the absorbent can be at least one of water and an organic solvent.
In a preferred embodiment of the present invention, the absorption system C further comprises a buffer tank located at a lower portion of the absorption apparatus and connected to the absorption apparatus for diluting the absorbent for easy discharge.
Wherein the absorbed absorbent can be separated from the resultant component in a manner known in the art and recycled, or can be discharged to a sewage treatment plant by adding a large amount of diluent (such as in the buffer tank) to reach the pollutant discharge standard.
[ poor cycle gas component control System D ]
The absorption system C absorbs the treated gas, which is defined as lean recycle gas, due to the consumption of part of the raw materials and the elimination of most of the product components by the previous reaction and absorption processes. The lean recycle gas also contains some CO and CO generated by the reaction but not absorbed by the absorption system C2And the by-products of the catalytic oxidation of the hydrocarbons can be gradually accumulated along with the content of the by-products in the circulation process if the by-products are not treated, and the data accuracy and the operation stability of the test device are seriously influenced. In order to solve the problem, the invention is provided with a lean cycle gas component regulation and control system D after the absorption system C, and the lean cycle gas after absorption and separation enters the system, so that a part of the by-products of the catalytic oxidation of the hydrocarbons can be discharged in time, and the purpose of regulating and controlling the components of the lean cycle gas is achieved.
As described above, the core of the present invention is that a lean recycle gas component regulation and control system D is introduced into the pilot plant test apparatus, and the lean recycle gas component regulation and control system D is introduced to solve the problem of accumulation of by-products such as carbon oxides existing in the existing apparatus, thereby truly achieving stable and accurate evaluation of the catalyst.
In a preferred embodiment of the present invention, the lean recycle gas component regulation and control system D includes a pressure vessel, one or more automatic discharge component regulation and control pipelines connected to the pressure vessel, one or more automatic discharge pressure regulation and control pipelines connected to the pressure vessel, and a pressure detection element disposed on the pressure vessel;
each automatic discharge component regulation and control pipeline is controlled by an instrument control system respectively, and the gas discharge amount is adjusted in real time according to the component analysis result fed back by online analysis;
each automatic discharge pressure regulation and control pipeline regulates the amount of discharged gas in real time according to the container pressure value fed back by the pressure detection element;
through setting up automatic component regulation and control pipeline of bleeding and automatic pressure regulation and control pipeline of bleeding, can make poor circulation gas component regulation and control system D can also guarantee the stability of test device pressure when satisfying poor circulation gas component regulation and control.
Wherein the number of the pressure containers is one or more; if the number of the pressure vessels is multiple, at least one of the pressure vessels is connected with one or more automatic discharge component regulating and controlling pipelines, at least one of the pressure vessels is connected with one or more automatic discharge pressure regulating and controlling pipelines, and at least one of the pressure vessels is provided with a pressure detection element.
Wherein, if a plurality of pressure vessels are provided, the pressure vessels are arranged in series.
Illustratively, the lean recycle gas component regulation and control system D comprises a pressure vessel, an automatic discharge component regulation and control pipeline connected with the pressure vessel, an automatic discharge pressure regulation and control pipeline, and a pressure detection element arranged on the pressure vessel.
Illustratively, the lean cycle gas component regulating system D comprises two pressure vessels, an automatic discharge component regulating and controlling line connected to one of the pressure vessels, an automatic discharge pressure regulating and controlling line connected to one of the pressure vessels or to the other of the pressure vessels, and a pressure detecting element disposed on one of the pressure vessels.
Wherein, the lean cycle gas after the components are regulated and controlled by the lean cycle gas component regulation and control system D is provided with power by the cycle compression system E and is circulated back to the raw material preparation system A.
[ circulation compression System E ]
In a preferred embodiment of the present invention, the cyclic compression system E comprises at least one compressor connected to the lean cycle gas component regulation system D and a buffer vessel connected to the feed distribution system a via the compressor.
The compressor is connected with a pressure container in the lean circulating gas component regulating and controlling system D, and the lean circulating gas treated by the lean circulating gas component regulating and controlling system D enters the buffer container through the compressor.
Wherein, the compressor can be selected from any type as long as the requirement of the process pressure can be met, and a diaphragm compressor is preferred.
Wherein, the buffer container connected with the compressor can eliminate the inherent pressure fluctuation caused by the operation of the compressor as much as possible.
Wherein, the compressed lean recycle gas is buffered by a buffer container and then returns to the raw material configuration system A through a process pipeline.
Wherein, the buffer container is also provided with a bypass which is directly connected with at least one pressure container of the lean circulating gas component regulating and controlling system D, and the buffer container is provided with a pressure detecting element.
An automatic control instrument is also arranged on the bypass, and the pressure of the device can be ensured to be more stable by taking the detection value of the pressure detection element on the buffer container as a feedback value.
[ Online analysis System F ]
Wherein the online analysis system F is connected with at least two systems of the raw material configuration system A, the reaction system B, the absorption system C, the lean cycle gas component regulation and control system D and the cycle compression system E.
In one embodiment, the on-line analysis system F is connected to at least two of the feed preparation system a, the reaction system B, and the lean recycle gas component control system D.
In one embodiment, the on-line analysis system F is connected to the feedstock distribution system a and the reaction system B.
In a preferred embodiment of the present invention, the on-line analysis system F comprises a sampling pipeline, an analysis instrument and a signal transmission line; the sampling pipeline is connected with an analytical instrument; the analysis instrument is connected with an instrument which needs to take the component analysis value as a control basis through a signal transmission line.
Wherein at least two systems of the raw material configuration system A, the reaction system B, the absorption system C, the lean cycle gas component regulation and control system D and the cycle compression system E are connected with sampling pipelines.
Wherein at least two systems of the raw material configuration system A, the reaction system B and the lean circulating gas component regulation and control system D are connected with sampling pipelines.
Wherein, the raw material configuration system A and the reaction system B are connected with a sampling pipeline.
Wherein the sampling line comprises sample pre-treatment equipment comprising a filter, a pressure-stabilizing valve, a flow meter, optionally components of free water content (such as a moisture separator).
In order to obtain more accurate analysis data, any component in the medium in the sampling pipeline should be prevented from being condensed and separated out, and the sampling pipeline can be provided with heat tracing in a steam or electric heating mode. The heat tracing and sampling lines may be wrapped together by insulation. The heat tracing temperature is in a certain range, the upper temperature limit is not higher than the thermal decomposition temperature of any component in the medium in the sampling pipeline, and the lower temperature limit is not lower than the condensation and precipitation temperature of any component in the medium in the pipeline.
The analyzer can be one or a combination of a plurality of analyzers, and the analyzer can be a gas chromatograph, a liquid chromatograph, an infrared analyzer, a magnetic oxygen analyzer, a mass spectrometer with a multi-channel switching valve, a plurality of single-channel mass spectrometers and the like.
The signal transmission line can timely and accurately transmit the analysis data of the analysis instrument to an instrument which needs to take the component analysis value as a control basis.
Preferably, the signal transmission line is connected with each instrument of the device through a signal control system, and the signal instrument control system can be a distributed control system, a programmable logic controller, a single chip system and other control systems which are provided with functions of collecting analog quantity signals and digital quantity signals, processing data and outputting the analog quantity signals and the digital quantity signals.
More preferably, the control system has a human-computer interaction interface, which is a software system, and can display various instrument signals transmitted by the device to an operator and output information input by the operator to the device. An operator can set the proportion of each component in the raw material by using the human-computer interaction interface, the signal control system can set the proportion of each component in the raw material according to the human-computer interaction interface, and the proportion of each component in the flow control system is automatically adjusted, so that the proportion of each component in the mixed raw material reaches the set value in the human-computer interaction interface.
Through the catalyst evaluation device of the technical scheme, the problem that the content of carbon oxides is effectively controlled while the accuracy and stability of evaluation data of the device are ensured by a circulating process can be solved.
The present invention will be described in further detail with reference to specific examples. It is to be understood that the following examples are only illustrative and explanatory of the present invention and should not be construed as limiting the scope of the present invention. All the technologies realized based on the above-mentioned contents of the present invention are covered in the protection scope of the present invention.
In the description of the present invention, it should be noted that the terms "first", "second", "third", etc. are used for descriptive purposes only and do not indicate or imply relative importance.
Example 1
A pilot test device for evaluating the performance of a catalyst for preparing ethylene oxide by ethylene epoxidation comprises a raw material preparation system A, a reaction system B, an absorption system C, a lean recycle gas component regulation and control system D, a recycle compression system E and an online analysis system F:
as shown in fig. 2, the feed distribution system a includes a mixer 104 for distributing the feed, the mixer 104 has three ports, a first port 101 is used for connecting to the feed gas pipeline and the recycling compression system E, a second port 102 is used for connecting to the oxidant pipeline, and a third port 103 is used for connecting to the reaction system B. During mixing, ethylene and nitrogen enter mixer 104 through the feed gas line, and oxygen enters mixer 104 through the oxidant line, where they are mixed in mixer 104. All the raw materials are uniformly mixed in a mixer 104 under the pressure stabilization and the quantitative accurate control of a mass flow controller 105, so that the content of each component reaches the reaction requirement.
The reaction system B has a reactor in which a reaction tube 106 is provided, and a catalyst sample 107 is deposited in the reaction tube 106, and the reaction tube is entirely immersed in a heat exchange medium desalting bath 111. A demineralised water bath 111 is contained in the heat exchange medium vessel and heat is supplied by the electric heater 108. A first thermocouple 109 and a second thermocouple 110 are respectively arranged in the desalted water bath inside the reaction tube 106 and outside the reaction tube 106, and the temperature of the catalyst bed layer and the temperature of the heat exchange medium are respectively monitored to ensure that the required temperatures can be reached. A pressure sensor 112 is provided in the heat exchange medium vessel for monitoring the pressure within the heat exchange medium vessel to prevent overpressure and damage to the vessel structure. The reaction tube 106 is made of 304 stainless steel, and the inner diameter of the reaction tube 106 is 31.3mm, and the equivalent diameter of the catalyst sample 107 stacked therein is not more than 9 mm. In order to prevent an overpressure situation during the reaction, a rupture disk 113 is installed at the upper end of the reaction tube 106.
The recycle gas containing ethylene, oxygen and nitrogen, which is provided by the raw material preparation system A, enters the reaction tube 106 from the upper end of the reactor and reacts with the catalyst sample 107 to generate ethylene oxide and CO as main productsxCarbon oxide by-products, flow out of the lower end of the reactor and enter the absorption system C through a line connected to the latter.
The absorption system C is composed of a filler absorption tower 114, the circulating gas containing main and side products from the reaction system B enters the filler absorption tower 114 from the middle part, desalted water flows down from the top of the tower as an absorbent and is in reverse contact with the circulating gas to absorb ethylene oxide components in the circulating gas and flows into a tower kettle, wherein a part of absorption liquid flows to a buffer tank, a large amount of water is simultaneously introduced into the tank, and the absorption liquid is diluted and analyzed to detect that the ethylene oxide concentration is not more than 50ppm, so that the ethylene oxide component can be discharged into a sewage treatment plant.
The lean recycle gas obtained after absorption treatment flows out of the top of the packed absorption tower 114 and enters a lean recycle gas component regulation and control system D, the system comprises a pressure vessel 115, the top of the pressure vessel 115 is provided with a pressure sensor 116, an automatic discharge pressure regulation and control pipeline 117 and an automatic discharge component regulation and control pipeline 118, the automatic discharge component regulation and control pipeline 118 adjusts the discharged gas quantity in real time through an instrument control system according to a COx analysis result fed back by online analysis, the automatic discharge pressure regulation and control pipeline 117 adjusts the discharged gas quantity in real time according to a vessel pressure value fed back by the pressure sensor 116, and the pressure stability of the whole evaluation device can be ensured while the regulation and control of the lean recycle gas components are met through the arrangement of the two pipelines.
The lean recycle gas after the components are regulated and controlled by the lean recycle gas component regulation and control system D is provided with power by the recycle compression system E and is recycled to the raw material preparation system A. The recycle compression system E has a diaphragm compressor 119 connected at its inlet to the outlet of the pressure vessel 115 of the lean recycle gas component conditioning system D via a line and at its outlet to a surge tank 120 which helps to eliminate the inherent pressure fluctuations associated with the operation of the compressor 119. The compressed lean recycle gas is buffered by the buffer tank 120 and returned to the first port 101 of the mixer 104 through the process line. The buffer vessel 120 is provided with a bypass 121 connected to the pressure vessel 115 of the lean recycle gas component regulation system D, and the buffer vessel 120 is further provided with a pressure sensor 122. The bypass 121 is provided with an automatic control instrument, and the detected value of the buffer container pressure sensor 122 is used as a feedback value, so that the pressure of the device can be ensured to be more stable.
Two sampling pipelines 123 are respectively led out from the pipeline connecting the raw material configuration system A and the reaction system B and the pipeline connecting the reaction system B and the absorption system C, and are connected with the on-line analysis system F. The on-line analysis system F includes a sampling line 123, a sample pre-treatment device 124, and a mass spectrometer 125 with a multi-channel switching valve. The sample pre-treatment device 124 is internally composed of a filter, a pressure stabilizing valve and a flow meter, and is also provided with a gas-liquid separator to reduce the content of free water. In order to obtain more accurate analysis data, any component in the medium in the sampling line should be prevented from being condensed out, and the sampling line 123 and the sample pre-treatment device 124 may be wrapped together with the sampling line by a heat insulating material with electric tracing. The heat tracing temperature can be controlled between 100 ℃ and 200 ℃.
The signal transmission line is connected with each instrument of the device through a Distributed Control System (DCS), so that the analysis data of the analysis instrument can be timely and accurately transmitted to the instruments which need to take the component analysis value as the control basis. The software system of the distributed control system is provided with a human-computer interaction interface, can display various instrument signals transmitted by the device to an operator, and can output information input by the operator to the device. An operator can set the proportion of each component in the raw material by using the human-computer interaction interface, the signal control system can set the proportion of each component in the raw material according to the human-computer interaction interface, and the proportion of each component in the flow control system is automatically adjusted, so that the proportion of each component in the mixed raw material reaches the set value in the human-computer interaction interface.
After detection, the device of example 1 is used for a catalyst pilot test, and the content of the carbon oxide detected by the detection is not more than 1.5 mol%, which is far lower than the range of 3-5 mol% of the content of the carbon oxide in the conventional device which is not regulated by the lean recycle gas component regulation and control system D.
The results show that the device is suitable for pilot-scale test evaluation experiments of low-carbon hydrocarbon oxidation catalysts, particularly pilot-scale test evaluation of catalysts for preparing ethylene oxide by oxidizing ethylene, and can effectively control the content of carbon oxides in a circulation process, so that the catalysts can be accurately and stably evaluated.
Example 2
A pilot test device for evaluating the performance of a catalyst for preparing ethylene oxide by ethylene epoxidation comprises a raw material preparation system A, a reaction system B, an absorption system C, a lean recycle gas component regulation and control system D, a recycle compression system E and an online analysis system F:
as shown in fig. 3, the feed distribution system a includes a mixer 204 for distributing the feed, the mixer 204 has three ports, a first port 201 is used for connecting to the feed gas pipeline and the recycling compression system E, a second port 202 is used for connecting to the oxidant pipeline, and a third port 203 is used for connecting to the reaction system B. During mixing, ethylene and nitrogen enter mixer 204 through the feed gas line and oxygen enters mixer 204 through the oxidant line, where they are mixed in mixer 204. All the raw materials are uniformly mixed in the mixer 204 under the pressure stabilization and the quantitative accurate control of the mass flow controller 205, so that the content of each component reaches the reaction requirement.
Reaction system B differs from example 1in that reaction system B has a reactor with 4 reaction tubes 206 and 209 stacked with different catalyst samples immersed in a heat conducting oil bath 214. The heat conducting oil bath 214 is contained in a heat exchange medium vessel having a jacket structure 211, heated by steam to provide heat. Thermocouples 212 and 213 are provided in the reactor tube and jacket, respectively, to monitor the temperature of the catalyst bed and the heat transfer medium to ensure that it reaches the desired temperature. The reaction tube is made of 304 stainless steel, the inner diameters of the reaction tube 206 and 209 are respectively 31.3mm, 39mm, 45mm and 1in, and the equivalent diameter of the catalyst sample 210 stacked therein is not more than 10 mm. In order to prevent an overpressure situation during the reaction, the lower end of the reaction tube is provided with a rupture disc 215.
The recycle gas containing ethylene, oxygen and nitrogen and configured by the raw material configuration system A enters a reaction tube 206-209 from the upper end of the reactor and reacts with a catalyst sample 210 to generate main products of ethylene oxide and COxCarbon oxide by-products, flow out of the lower end of the reactor and enter the absorption system C through a line connected to the latter.
The absorption system C is composed of a plate type absorption tower 216, the circulating gas containing main and side products from the reaction system B enters the plate type absorption tower 216 from the middle part, tap water as an absorbent flows down from the top of the tower and is in reverse contact with the circulating gas to absorb ethylene oxide components in the circulating gas and flows into a tower kettle, a part of absorption liquid flows to a buffer tank, a large amount of water is simultaneously introduced into the buffer tank, and the absorption liquid is diluted and analyzed to detect that the ethylene oxide concentration of the absorption liquid is not more than 50ppm, so that the absorption liquid can be discharged into a sewage treatment plant.
The lean recycle gas after absorption treatment flows out from the top of the plate-type absorption tower 216 and enters a lean recycle gas component regulation and control system D, which comprises two pressure vessels connected in series, wherein the top of the first pressure vessel 217 is provided with an automatic discharge component regulation and control pipeline 219, the top of the second pressure vessel 218 is provided with an automatic discharge pressure regulation and control pipeline 220 and a pressure sensor 221. The first pressure vessel's automatic bleed component control line 219 passes through the instrument control system and analyzes the fed back CO on-linexAnalysis of the results, real-time adjustment of the amount of gas bled, automation of the second pressure vessel 218The discharge pressure regulating and controlling pipeline 220 regulates the amount of discharged gas in real time according to the container pressure value fed back by the pressure sensor 221, so that the pressure stability of the whole evaluation device can be ensured while the poor cycle gas component is regulated and controlled.
The lean recycle gas after the components are regulated and controlled by the lean recycle gas component regulation and control system D is provided with power by the recycle compression system E and is recycled to the raw material preparation system A. The recycle compression system E has a diaphragm compressor 222 connected at its inlet to the outlet of the second pressure vessel 218 of the lean recycle gas component conditioning system D via a line and at its outlet to a surge tank 223 which helps to eliminate the inherent pressure fluctuations associated with the operation of the compressor 222. The compressed lean recycle gas is buffered by the buffer tank 223 and returned to the first port 201 of the mixer 104 through the process line.
The buffer vessel 223 is provided with a bypass 224 to the pressure vessel 218 of the lean recycle gas component regulation system D, and the buffer vessel 223 is further provided with a pressure sensor 225. The bypass 224 is provided with an automatic control instrument, and the detected value of the buffer container pressure detecting element is used as a feedback value, so that the pressure of the device can be ensured to be more stable.
Two sampling pipelines 226 are respectively led out from the pipeline connecting the reaction system B and the absorption system C and the pipeline connecting the absorption system C and the lean circulating gas component regulation system D and are connected with the on-line analysis system F. The on-line analysis system F includes a sampling line 226, a sample pre-treatment device 227, and an on-line gas chromatograph 228 with a multi-channel switching valve. The sample pretreatment device 227 is internally composed of a filter, a pressure stabilizing valve and a flowmeter, and is also provided with a gas-liquid separator to reduce the content of free water. In order to obtain more accurate analysis data, any component in the medium in the sampling line should be prevented from being condensed out, and the sampling line 226 and the sample pre-treatment device 227 may be wrapped together with the sampling line by a heat insulating material with electric tracing. The heat tracing temperature can be controlled between 100 ℃ and 200 ℃.
The signal transmission line is connected with each instrument of the device through a programmable logic controller, and can timely and accurately transmit the analysis data of the analysis instrument to the instruments which need to take the component analysis value as the control basis. The software system of the programmable logic controller is provided with a human-computer interaction interface, can display various instrument signals transmitted by the device to an operator, and can output information input by the operator to the device. An operator can set the proportion of each component in the raw material by using the human-computer interaction interface, the signal control system can set the proportion of each component in the raw material according to the human-computer interaction interface, and the proportion of each component in the flow control system is automatically adjusted, so that the proportion of each component in the mixed raw material reaches the set value in the human-computer interaction interface.
After detection, the device of example 2 is used for a catalyst pilot test, and the content of the carbon oxide detected by the detection is not more than 1.4 mol%, which is far lower than the content of the carbon oxide in the conventional device which is not regulated by the lean recycle gas component regulation and control system D by 3-5 mol%.
The results show that the device is suitable for pilot-scale test evaluation experiments of low-carbon hydrocarbon oxidation catalysts, particularly pilot-scale test evaluation of catalysts for preparing ethylene oxide by oxidizing ethylene, and can effectively control the content of carbon oxides in a circulation process, so that the catalysts can be accurately and stably evaluated.
The embodiments of the present invention have been described above. However, the present invention is not limited to the above embodiment. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (10)
1. A pilot test device for evaluating the performance of a low-carbon hydrocarbon oxidation catalyst comprises a raw material preparation system, a reaction system, an absorption system, a lean cycle gas component regulation and control system, a cycle compression system and an online analysis system;
the raw material configuration system, the reaction system, the absorption system, the lean circulating gas component regulation and control system and the circulating compression system are sequentially connected and combined into a closed loop;
the on-line analysis system is connected with at least two systems of the raw material configuration system, the reaction system, the absorption system, the lean cycle gas component regulation and control system and the cycle compression system.
2. The apparatus of claim 1, wherein the feed preparation system is configured to prepare the feed gas mixture according to the content requirements of the feed components in the process conditions;
the reaction system is used for realizing catalytic reaction of the catalyst sample;
the absorption system is used for absorbing the target product generated by the reaction system;
the lean cycle gas component regulation and control system is used for regulating and controlling the content of carbon oxide components in the lean cycle gas;
the circulation compression system is used for returning the lean circulation gas to the raw material configuration system;
the on-line analysis system is used for analyzing the component content of the circulating gas on line so as to adjust and control the composition of the circulating gas and obtain catalyst reaction data.
3. The apparatus of claim 1 or 2, wherein the feedstock distribution system comprises a mixer for distributing the feedstock, the mixer comprising at least three ports, a first port, a second port and a third port, the first port being connected to the feed gas conduit and the recycle compression system, respectively, the second port being connected to the oxidant conduit, and the third port being connected to the reaction system.
4. The apparatus of any one of claims 1-3, wherein the reaction system comprises a reactor comprising a reaction tube, a heater, a heat exchange medium vessel, a first temperature measuring element, and a pressure sensing element;
wherein the reaction tube is arranged in a heat exchange medium container; the heat exchange medium container is filled with a heat exchange medium; the first temperature measuring element is used for monitoring the temperature of the heat exchange medium in the heat exchange medium container so as to ensure that the heat exchange medium can reach the required temperature; the pressure detection element is used for monitoring the pressure in the heat exchange medium container and preventing overpressure from damaging the container structure; the heater is used for providing heat for the heat exchange medium.
Preferably, the reaction tube further comprises a member capable of rapid pressure relief.
5. The apparatus of any one of claims 1-4, wherein the reaction system further comprises a second temperature sensing element; the second temperature measuring element is used for measuring the temperature of the reaction tube.
Preferably, the second temperature measuring element is arranged at any one or more positions of the outer side, the inner side and the like of the reaction tube.
For example, the second temperature measuring element is one and is arranged on the inner side of the reaction tube;
or the number of the second temperature measuring elements is two, one of the second temperature measuring elements is arranged on the inner side of the reaction tube, and the other one is arranged on the outer side of the reaction tube;
or the number of the second temperature measuring elements is three, one of the second temperature measuring elements is arranged on the inner side of the reaction tube, the second temperature measuring element is arranged on the outer side of the reaction tube, and the third temperature measuring element is arranged on the surface of the heater.
6. The apparatus of any one of claims 1-5, wherein the absorption system comprises one or more absorption devices to ensure complete absorption of the product components in the reacted gas.
Preferably, when the absorption device is a plurality of absorption devices, the absorption devices can be arranged in series or in parallel, and the absorption devices are preferably arranged in series.
Preferably, the absorption system further comprises a buffer tank located at a lower portion of the absorption apparatus and connected to the absorption apparatus for diluting the absorbent.
7. The apparatus of any of claims 1-6, wherein the lean cycle gas component regulation system comprises a pressure vessel, one or more automatic bleed component regulation lines connected to the pressure vessel, one or more automatic bleed pressure regulation lines connected to the pressure vessel, and a pressure sensing element disposed on the pressure vessel;
each automatic discharge component regulation and control pipeline is controlled by an instrument control system respectively, and the gas discharge amount is adjusted in real time according to the component analysis result fed back by online analysis;
and each automatic discharge pressure regulation and control pipeline regulates the amount of discharged gas in real time according to the pressure value of the container fed back by the pressure detection element.
8. The apparatus of any one of claims 1-7, wherein the number of pressure vessels is one or more; if the number of the pressure vessels is multiple, at least one of the pressure vessels is connected with one or more automatic discharge component regulating and controlling pipelines, at least one of the pressure vessels is connected with one or more automatic discharge pressure regulating and controlling pipelines, and at least one of the pressure vessels is provided with a pressure detection element.
Preferably, the lean recycle gas component regulation and control system comprises a pressure vessel, an automatic discharge component regulation and control pipeline connected with the pressure vessel, an automatic discharge pressure regulation and control pipeline and a pressure detection element arranged on the pressure vessel.
Preferably, the lean recycle gas component regulation and control system comprises two pressure vessels, an automatic discharge component regulation and control pipeline connected with one of the pressure vessels, an automatic discharge pressure regulation and control pipeline connected with one of the pressure vessels or with the other of the pressure vessels, and a pressure detection element arranged on one of the pressure vessels.
Preferably, the lean recycle gas after the components are regulated and controlled by the lean recycle gas component regulation and control system is provided with power by the recycle compression system and is recycled to the raw material configuration system.
9. The apparatus of any one of claims 1-8, wherein the cyclic compression system comprises at least one compressor coupled to the lean cycle gas component conditioning system and a surge vessel coupled to the feed distribution system via the compressor.
Preferably, the compressor is connected with a pressure vessel in the lean recycle gas component regulation and control system, and the lean recycle gas treated by the lean recycle gas component regulation and control system enters the buffer vessel through the compressor.
Preferably, the buffer container is also provided with a bypass, the bypass is directly connected with at least one pressure container of the lean circulating gas component regulation system, and the buffer container is provided with a pressure detection element.
10. The apparatus of any one of claims 1-9, wherein the on-line analysis system is coupled to at least two of the feed configuration system, the reaction system, the absorption system, the lean cycle gas component conditioning system, and the recycle compression system.
Preferably, the on-line analysis system is connected with at least two systems of the raw material configuration system, the reaction system and the lean recycle gas component regulation and control system.
Preferably, the on-line analysis system is connected with the raw material preparation system and the reaction system.
Preferably, the on-line analysis system comprises a sampling pipeline, an analysis instrument and a signal transmission line; the sampling pipeline is connected with an analytical instrument; the analysis instrument is connected with an instrument which needs to take the component analysis value as a control basis through a signal transmission line.
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