CN204576212U - Pressure-variable adsorption agent regenerating control device - Google Patents
Pressure-variable adsorption agent regenerating control device Download PDFInfo
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- CN204576212U CN204576212U CN201520032944.7U CN201520032944U CN204576212U CN 204576212 U CN204576212 U CN 204576212U CN 201520032944 U CN201520032944 U CN 201520032944U CN 204576212 U CN204576212 U CN 204576212U
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Abstract
The utility model belongs to a kind of pressure-variable adsorption agent regenerating control device; Comprise multimedium admission gear, flusher, emptier and control system, multimedium admission gear comprises nitrogen inlet, hydrogen inlet and qualified purified gas air intake opening; Flusher comprises nitrogen buffer tank, hydrogen gas buffer and qualified purified gas surge tank; Emptier comprises and is located at vacuum pump and emptying house steward, and described vacuum pump is connected by pipeline with emptying house steward; Control system comprises model predictive controller, DCS main control card and DCS database; Have reasonable in design, the variation of adsorbent reactivation mode, Automated condtrol ability is strong, and available gas yield is large, energy-saving and emission-reduction, is applicable to the advantage of producing that maximizes.
Description
Technical field
The utility model belongs to sorbent regeneration technology field, is specifically related to a kind of pressure-variable adsorption agent regenerating control device.
Background technology
Pressure swing adsorption (Pressure Swing Adsorption. is called for short PSA) is the gas separation of industrially new emergence in recent decades, is physical chemistry seepage theory embody rule industrially.
At present, pressure swing adsorption has formed an important industry, is widely used at gas separaion and field of purification.Within from now on period, pressure swing adsorption will occupy very large ratio.Adsorbent reactivation is the important process of pressure swing adsorption one, and regeneration can adopt and find time and the mode such as flushing, process recovers of finding time is thorough, but energy consumption is high; Developing technique energy consumption is low, but requires high to scouring media purity and adsorbability and have the problems such as part remains to bring very large puzzlement to enterprise.Therefore how the energy-saving transformation absorbing process system of finding time and the technological advantage of developing technique combines is become the active demand of enterprise.
Utility model content
The purpose of this utility model is to overcome defect of the prior art and provides a kind of reasonable in design, the variation of adsorbent reactivation mode, and Automated condtrol ability is strong, and available gas yield is large, is applicable to the pressure-variable adsorption agent regenerating control device produced that maximizes.
The purpose of this utility model is achieved in that this regenerating control device comprises multimedium admission gear, flusher, emptier and control system,
A, multimedium admission gear comprise nitrogen inlet, hydrogen inlet and qualified purified gas air intake opening; Nitrogen inlet is connected with the nitrogen buffer tank import on nitrogen air inlet pressure sensor, nitrogen air inlet adjustment valve and flusher successively by pipeline, hydrogen inlet is connected with the hydrogen gas buffer import on hydrogen gas pressure transducer, hydrogen gas variable valve and flusher successively by pipeline, and qualified purified gas air intake opening is connected with the qualified purified gas surge tank import on qualified purified gas air inlet pressure sensor, qualified purified gas air inlet adjustment valve and flusher successively by pipeline;
B, flusher comprise nitrogen buffer tank, hydrogen gas buffer and qualified purified gas surge tank, nitrogen buffer tank outlet by pipeline successively with nitrogen wash variable valve, nitrogen flow meter is connected with nitrogen pressure sensor, nitrogen pressure sensor is connected with the nitrogen wash sequencing valve that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged respectively, hydrogen gas buffer outlet rinses variable valve with hydrogen successively by pipeline, hydrogen flowmeter and hydrogen gas pressure sensor, hydrogen gas pressure sensor rinses sequencing valve with the hydrogen that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged respectively and is connected, qualified purified gas surge tank outlet rinses variable valve with qualified purified gas successively by pipeline, qualified purifying gas flow gauge and qualified purified gas pressure transducer, qualified purified gas pressure transducer rinses sequencing valve with the qualified purified gas that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged respectively and is connected, the qualified purified gas that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged sequencing valve components analysis instrument of giving vent to anger with qualified purified gas respectively of giving vent to anger is connected, described qualified purified gas components analysis instrument of giving vent to anger is connected with qualified purified gas air intake opening by pipeline, described at least two group adsorption tower unit adsorbent reactivation stage gas outlets are provided with unstripped gas sequencing valve be connected with raw material gas inlet respectively, at least two group adsorption tower unit adsorbent reactivation stage gas outlets are provided with the first threeway respectively and between corresponding unstripped gas sequencing valve, 3rd end of the first threeway is connected with the emptying house steward in emptier by purge gas sequencing valve of giving vent to anger, 3rd end of the first threeway and purge gas are given vent to anger between sequencing valve and are provided with the second threeway, 3rd end of the second threeway is connected with the vacuum pump in emptier by exhaust sequencing valve, described qualified purified gas air intake opening uses workshop section to be connected with back segment purified gas, at least be provided with an adsorption tower respectively in described at least two group adsorption tower unit, described adsorption tower is provided with adsorption column pressure sensor,
C, emptier comprise and are located at vacuum pump and emptying house steward, and described vacuum pump is connected by pipeline with emptying house steward;
D, control system comprises model predictive controller, DCS main control card and DCS database, described nitrogen air inlet pressure sensor, hydrogen gas pressure transducer, qualified purified gas air inlet pressure sensor, nitrogen flow meter, nitrogen pressure sensor, hydrogen flowmeter, hydrogen gas pressure sensor, qualified purifying gas flow gauge, qualified purified gas pressure transducer, adsorption column pressure sensor and qualified purified gas components analysis instrument of giving vent to anger is connected with DCS database respectively by data line, DCS database is connected with model predictive controller by DCS main control card, model predictive controller controls nitrogen air inlet adjustment valve by DCS main control card, hydrogen gas variable valve, qualified purified gas air inlet adjustment valve, nitrogen wash variable valve, nitrogen wash sequencing valve, hydrogen rinses variable valve, hydrogen rinses sequencing valve, qualified purified gas rinses variable valve, qualified purified gas rinses sequencing valve, purge gas is given vent to anger sequencing valve, vacuum pump and exhaust sequencing valve.Described often group between adsorption tower unit adopts mode in parallel to be connected.
The utility model is by arranging nitrogen buffer tank, hydrogen gas buffer, qualified purified gas surge tank, various detection and actuating unit, not only can reach the switching of various flushing regeneration, and can ensure with the object of the vacuum pump out of service in for the pressure swing adsorption of regeneration of finding time, for 24 tower pressure swing adsorptions, 6, pressure-variable adsorption two sections of 160KW vacuum pumps run the technological requirement that just can reach adsorbent reactivation, after rinsing method of reproduction as switched to, 6 vacuum pumps can be all out of service, as required, process conditions are harsh, mixed regeneration method of rinsing and find time can be carried out, namely after flushing regeneration completes, a vacuum pump is utilized to carry out regeneration of finding time, such adsorbent reactivation is comparatively thorough.Can save the electricity charge about 2,280,000 yuan every year as run according to flushing and mixed regeneration method of finding time, concrete computation process is 160*0.8 (electric efficiency calculates according to 0.8) * 5*24*330 (working time in year calculated according to 330 days) * 0.45 (electricity price is adjusted according to 0.45 yuan)=2,280,000 yuan; The utility model has reasonable in design, the variation of adsorbent reactivation mode, and Automated condtrol ability is strong, and available gas yield is large, energy-saving and emission-reduction, is applicable to the advantage of producing that maximizes.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of the utility model adsorption tower;
Fig. 3 is control system block diagram of the present utility model.
Embodiment
As shown in Figure 1, 2, 3, the utility model is pressure-variable adsorption agent regenerating control device, and this regenerating control device comprises multimedium admission gear, flusher, emptier and control system,
A, multimedium admission gear comprise nitrogen inlet 1, hydrogen inlet 5 and qualified purified gas air intake opening 9; Nitrogen inlet 1 is connected with nitrogen buffer tank 4 import on nitrogen air inlet pressure sensor 2, nitrogen air inlet adjustment valve 3 and flusher successively by pipeline, hydrogen inlet 5 is connected with hydrogen gas buffer 8 import on hydrogen gas pressure transducer 6, hydrogen gas variable valve 7 and flusher successively by pipeline, and qualified purified gas air intake opening 9 is connected with qualified purified gas surge tank 12 import on qualified purified gas air inlet pressure sensor 10, qualified purified gas air inlet adjustment valve 11 and flusher successively by pipeline;
B, flusher comprise nitrogen buffer tank 4, hydrogen gas buffer 8 and qualified purified gas surge tank 12, nitrogen buffer tank 4 export by pipeline successively with nitrogen wash variable valve 14, nitrogen flow meter 15 is connected with nitrogen pressure sensor 16, nitrogen pressure sensor 16 is connected with the nitrogen wash sequencing valve 17 that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged respectively, hydrogen gas buffer 8 exports and rinses variable valve 20 with hydrogen successively by pipeline, hydrogen flowmeter 21 and hydrogen gas pressure sensor 22, hydrogen gas pressure sensor 22 rinses sequencing valve 23 with the hydrogen that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged respectively and is connected, qualified purified gas surge tank 12 exports and rinses variable valve 25 with qualified purified gas successively by pipeline, qualified purifying gas flow gauge 26 and qualified purified gas pressure transducer 27, qualified purified gas pressure transducer 27 rinses sequencing valve 28 with the qualified purified gas that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged respectively and is connected, the qualified purified gas that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged sequencing valve 19 components analysis instrument 24 of giving vent to anger with qualified purified gas respectively of giving vent to anger is connected, described qualified purified gas components analysis instrument 24 of giving vent to anger is connected with qualified purified gas air intake opening 9 by pipeline, described at least two group adsorption tower unit adsorbent reactivation stage gas outlets are provided with unstripped gas sequencing valve 30 be connected with raw material gas inlet 29 respectively, at least two group adsorption tower unit adsorbent reactivation stage gas outlets respectively and be provided with the first threeway 40 between corresponding unstripped gas sequencing valve 30, 3rd end of the first threeway 40 is connected with the emptying house steward 33 in emptier by purge gas sequencing valve 32 of giving vent to anger, 3rd end of the first threeway 40 and purge gas are given vent to anger between sequencing valve 32 and are provided with the second threeway 34, 3rd end of the second threeway 34 is connected with the vacuum pump 36 in emptier by exhaust sequencing valve 35, described qualified purified gas air intake opening 9 uses workshop section to be connected with back segment purified gas, at least be provided with an adsorption tower 18 respectively in described at least two group adsorption tower unit, described adsorption tower 18 is provided with adsorption column pressure sensor 13,
C, emptier comprise and are located at vacuum pump 36 and emptying house steward 33, and described vacuum pump 36 is connected by pipeline with emptying house steward 33;
D, control system comprises model predictive controller 37, DCS main control card 38 and DCS database 39, described nitrogen air inlet pressure sensor 2, hydrogen gas pressure transducer 6, qualified purified gas air inlet pressure sensor 10, nitrogen flow meter 15, nitrogen pressure sensor 16, hydrogen flowmeter 21, hydrogen gas pressure sensor 22, qualified purifying gas flow gauge 26, qualified purified gas pressure transducer 27, adsorption column pressure sensor 13 and qualified purified gas components analysis instrument 24 of giving vent to anger is connected with DCS database 39 respectively by data line, DCS database 39 is connected with model predictive controller 37 by DCS main control card 38, and model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38, hydrogen gas variable valve 7, qualified purified gas air inlet adjustment valve 11, nitrogen wash variable valve 14, nitrogen wash sequencing valve 17, hydrogen rinses variable valve 20, hydrogen rinses sequencing valve 23, qualified purified gas rinses variable valve 25, qualified purified gas rinses sequencing valve 28, purge gas is given vent to anger sequencing valve 32, vacuum pump 36 and exhaust sequencing valve 35.Described often group between adsorption tower unit adopts mode in parallel to be connected.
Two groups of adsorption tower unit are had at least in the utility model, wherein one group of adsorption tower unit is in operation absorption phase, other one group of adsorption tower unit is used for the adsorbent reactivation stage, when wherein one group of adsorption tower unit by run absorption phase transfer the adsorbent reactivation stage to time, adopt nitrogen wash renovation process, hydrogen rinses renovation process, and qualified purified gas rinses renovation process, renovation process is rinsed in mixing, the mixed regeneration method or vacuumize method of reproduction and regenerate of rinsing and find time:
The utility model adopts nitrogen wash renovation process to regenerate adsorption tower unit adsorbent reactivation, comprises the steps:
Step one: nitrogen wash preparatory stage, when nitrogen air inlet pressure sensor 2 detects that nitrogen pressure is between 0.2 ~ 0.4MPa, nitrogen air inlet pressure sensor 2 will detect that nitrogen pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, and model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38 and nitrogen wash variable valve 14 is opened; Described nitrogen air inlet adjustment valve 3 aperture is 80%, and nitrogen wash variable valve 14 aperture is 80%, and the flow of nitrogen is 4000Nm
3/ h;
Step 2: enter the nitrogen wash stage, after the valve of nitrogen air inlet adjustment described in above-mentioned steps one 3 and nitrogen wash variable valve 14 are opened, model predictive controller 37 controls nitrogen wash sequencing valve 17 by DCS main control card 38 and opens, the aperture of described nitrogen wash sequencing valve 17 is 100%, and nitrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage; Its flushing adsorbent duration is: 488s;
Step 3: enter the nitrogen purge stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps two, model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38, nitrogen wash variable valve 14 and nitrogen wash sequencing valve 17 are closed, open purge gas to give vent to anger sequencing valve 32 simultaneously, make nitrogen wash gas be sent to blowing-air recovery heat by emptying house steward 32;
Step 4: the adsorption tower 18 in the adsorption tower unit in above-mentioned adsorbent reactivation stage enters absorption phase, open unstripped gas sequencing valve 30 and qualified purified gas to give vent to anger sequencing valve 19, unstripped gas enters in the adsorption tower unit of above-mentioned absorption phase by unstripped gas sequencing valve 30, after adsorption tower 18 adsorbs, qualified purified gas enters qualified purified gas air intake opening 9 by qualified purified gas sequencing valve 19 and qualified purified gas components analysis instrument 24 of giving vent to anger of giving vent to anger, and now qualified purified gas components analysis instrument 24 of giving vent to anger carries out gas analysis to qualified purified gas;
Step 5: when the components analysis instrument 24 of giving vent to anger of the qualified purified gas described in above-mentioned steps four carries out gas analysis to qualified purified gas, wherein nitrogen content be less than 20% and carbon dioxide content is less than 1.5% time, after the adsorption tower 18 entered described in step 4 in the adsorption tower unit of absorption phase enters the adsorbent reactivation stage, step one, step 2 and step 3 in nitrogen wash renovation process is adopted to carry out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage.
The utility model adopts nitrogen wash renovation process to regenerate adsorption tower unit adsorbent reactivation, comprises the steps:
Step one: nitrogen wash preparatory stage, when nitrogen air inlet pressure sensor 2 detects that nitrogen pressure is between 0.2 ~ 0.4MPa, nitrogen air inlet pressure sensor 2 will detect that nitrogen pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, and model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38 and nitrogen wash variable valve 14 is opened; Described nitrogen air inlet adjustment valve 3 aperture is 80%, and nitrogen wash variable valve 14 aperture is 80%, and the flow of nitrogen is 4000Nm
3/ h;
Step 2: enter the nitrogen wash stage, after the valve of nitrogen air inlet adjustment described in above-mentioned steps one 3 and nitrogen wash variable valve 14 are opened, model predictive controller 37 controls nitrogen wash sequencing valve 17 by DCS main control card 38 and opens, the aperture of described nitrogen wash sequencing valve 17 is 100%, and nitrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage; Its flushing adsorbent duration is: 488s;
Step 3: enter the nitrogen purge stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps two, model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38, nitrogen wash variable valve 14 and nitrogen wash sequencing valve 17 are closed, open purge gas to give vent to anger sequencing valve 32 simultaneously, make nitrogen wash gas be sent to blowing-air recovery heat by emptying house steward 32;
Step 4: the adsorption tower 18 in the adsorption tower unit in above-mentioned adsorbent reactivation stage enters absorption phase, open unstripped gas sequencing valve 30 and qualified purified gas to give vent to anger sequencing valve 19, unstripped gas enters in the adsorption tower unit of above-mentioned absorption phase by unstripped gas sequencing valve 30, after adsorption tower 18 adsorbs, qualified purified gas enters qualified purified gas air intake opening 9 by qualified purified gas sequencing valve 19 and qualified purified gas components analysis instrument 24 of giving vent to anger of giving vent to anger, and now qualified purified gas components analysis instrument 24 of giving vent to anger carries out gas analysis to qualified purified gas;
Step 5: when the components analysis instrument 24 of giving vent to anger of the qualified purified gas described in above-mentioned steps four carries out gas analysis to qualified purified gas, wherein nitrogen content is not less than 20% or carbon dioxide content when being not less than 1.5%, after the adsorption tower 18 entered described in step 4 in the adsorption tower unit of absorption phase enters the adsorbent reactivation stage, when nitrogen air inlet pressure sensor 2 detects that nitrogen pressure is between 0.2 ~ 0.4MPa, nitrogen air inlet pressure sensor 2 will detect that nitrogen pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38 and nitrogen wash variable valve 14 is opened, described nitrogen air inlet adjustment valve 3 aperture is 80%, and nitrogen wash variable valve 14 aperture is 80%, and the flow of nitrogen is 4000Nm
3/ h,
Step 6: again enter the nitrogen wash stage, after the valve of nitrogen air inlet adjustment described in above-mentioned steps five 3 and nitrogen wash variable valve 14 are opened, model predictive controller 37 controls nitrogen wash sequencing valve 17 by DCS main control card 38 and opens, the aperture of described nitrogen wash sequencing valve 17 is 100%, and nitrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage; Its flushing adsorbent duration is: 350s;
Step 7: enter again the nitrogen purge stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps six, analysis data are fed back to model predictive controller 37 by DCS database 39 and DCS main control card 38 by qualified purified gas components analysis instrument 24 of giving vent to anger, model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38, nitrogen wash variable valve 14 and nitrogen wash sequencing valve 17 are closed, make vacuum pump 36 open and open exhaust sequencing valve 35 simultaneously, evacuation processes is carried out to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, the nitrogen wash gas of evacuation processes is sent to blowing-air recovery heat by emptying house steward 32, the time of described evacuation processes is: 50s.
The utility model adopts hydrogen flushing renovation process to regenerate adsorption tower unit adsorbent reactivation, comprises the steps:
Step one: hydrogen rinses the preparatory stage, when hydrogen gas pressure transducer 6 detects that Hydrogen Vapor Pressure is between 0.2 ~ 0.4MPa, hydrogen gas pressure transducer 6 will detect that Hydrogen Vapor Pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38 and hydrogen flushing variable valve 20 is opened, described hydrogen gas variable valve 7 aperture is 80%, the aperture that hydrogen rinses variable valve 20 is 80%, and the flow of hydrogen is 3200Nm
3/ h;
Step 2: enter hydrogen rinse stage, after hydrogen gas variable valve 7 described in above-mentioned steps one and hydrogen rinse variable valve 20 unlatching, model predictive controller 37 controls hydrogen flushing sequencing valve 23 by DCS main control card 38 and opens, the aperture that described hydrogen rinses sequencing valve 23 is 100%, hydrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 400s;
Step 3: enter hydrogen empty stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps two, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38, hydrogen rinses variable valve 20 and hydrogen flushing sequencing valve 23 cuts out, open purge gas to give vent to anger sequencing valve 32 simultaneously, make hydrogen purge gas be sent to blowing-air recovery heat by emptying house steward 32;
Step 4: the adsorption tower 18 in the adsorption tower unit in above-mentioned adsorbent reactivation stage enters absorption phase, open unstripped gas sequencing valve 30 and qualified purified gas to give vent to anger sequencing valve 19, unstripped gas enters in the adsorption tower unit of above-mentioned absorption phase by unstripped gas sequencing valve 30, after adsorption tower 18 adsorbs, qualified purified gas enters qualified purified gas air intake opening 9 by qualified purified gas sequencing valve 19 and qualified purified gas components analysis instrument 24 of giving vent to anger of giving vent to anger, and now qualified purified gas components analysis instrument 24 of giving vent to anger carries out gas analysis to qualified purified gas;
Step 5: when the components analysis instrument 24 of giving vent to anger of the qualified purified gas described in above-mentioned steps four carries out gas analysis to qualified purified gas, when wherein carbon dioxide content is less than 1.5%, after the adsorption tower 18 entered described in step 4 in the adsorption tower unit of absorption phase enters the adsorbent reactivation stage, the step one, step 2 and the step 3 that adopt hydrogen to rinse in renovation process carry out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage.
The utility model adopts hydrogen flushing renovation process to regenerate adsorption tower unit adsorbent reactivation, comprises the steps:
Step one: hydrogen rinses the preparatory stage, when hydrogen gas pressure transducer 6 detects that Hydrogen Vapor Pressure is between 0.2 ~ 0.4MPa, hydrogen gas pressure transducer 6 will detect that Hydrogen Vapor Pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38 and hydrogen flushing variable valve 20 is opened, described hydrogen gas variable valve 7 aperture is 80%, the aperture that hydrogen rinses variable valve 20 is 80%, and the flow of hydrogen is 3200Nm
3/ h;
Step 2: enter hydrogen rinse stage, after hydrogen gas variable valve 7 described in above-mentioned steps one and hydrogen rinse variable valve 20 unlatching, model predictive controller 37 controls hydrogen flushing sequencing valve 23 by DCS main control card 38 and opens, the aperture that described hydrogen rinses sequencing valve 23 is 100%, hydrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 400s;
Step 3: enter hydrogen empty stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps two, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38, hydrogen rinses variable valve 20 and hydrogen flushing sequencing valve 23 cuts out, open purge gas to give vent to anger sequencing valve 32 simultaneously, make hydrogen purge gas be sent to blowing-air recovery heat by emptying house steward 32;
Step 4: the adsorption tower 18 in the adsorption tower unit in above-mentioned adsorbent reactivation stage enters absorption phase, open unstripped gas sequencing valve 30 and qualified purified gas to give vent to anger sequencing valve 19, unstripped gas enters in the adsorption tower unit of above-mentioned absorption phase by unstripped gas sequencing valve 30, after adsorption tower 18 adsorbs, qualified purified gas enters qualified purified gas air intake opening 9 by qualified purified gas sequencing valve 19 and qualified purified gas components analysis instrument 24 of giving vent to anger of giving vent to anger, and now qualified purified gas components analysis instrument 24 of giving vent to anger carries out gas analysis to qualified purified gas;
Step 5: when the components analysis instrument 24 of giving vent to anger of the qualified purified gas described in above-mentioned steps four carries out gas analysis to qualified purified gas, when wherein carbon dioxide content is not less than 1.5%, after the adsorption tower 18 in the adsorption tower unit entering absorption phase described in step 4 enters the adsorbent reactivation stage, when hydrogen gas pressure transducer 6 detects that Hydrogen Vapor Pressure is between 0.2 ~ 0.4MPa, hydrogen gas pressure transducer 6 will detect that Hydrogen Vapor Pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38 and hydrogen flushing variable valve 20 is opened, described hydrogen gas variable valve 7 aperture is 80%, the aperture that hydrogen rinses variable valve 20 is 80%, the flow of hydrogen is 3200Nm
3/ h,
Step 6: again enter hydrogen rinse stage, after hydrogen gas variable valve 7 described in above-mentioned steps five and hydrogen rinse variable valve 20 unlatching, model predictive controller 37 controls hydrogen flushing sequencing valve 23 by DCS main control card 38 and opens, the aperture that described hydrogen rinses sequencing valve 23 is 100%, hydrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 350s;
Step 7: enter hydrogen empty stage again, when rinsing after adsorbent reactivation terminates described in above-mentioned steps six, analysis data are fed back to model predictive controller 37 by DCS database 39 and DCS main control card 38 by qualified purified gas components analysis instrument 24 of giving vent to anger, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38, hydrogen rinses variable valve 20 and hydrogen flushing sequencing valve 23 cuts out, make vacuum pump 36 open and open exhaust sequencing valve 35 simultaneously, evacuation processes is carried out to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, the hydrogen purge gas of evacuation processes is sent to blowing-air recovery heat by emptying house steward 32, the time of described evacuation processes is: 50s.
The utility model adopts qualified purified gas flushing renovation process to regenerate adsorption tower unit adsorbent reactivation, comprises the steps:
Step one: qualified purified gas rinses the preparatory stage, when qualified purified gas air inlet pressure sensor 10 detects that Hydrogen Vapor Pressure is between 0.2 ~ 0.4MPa, qualified purified gas air inlet pressure sensor 10 will detect that qualified purified gas pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls qualified purified gas air inlet adjustment valve 11 by DCS main control card 38 and qualified purified gas flushing variable valve 25 is opened, described qualified purified gas air inlet adjustment valve 11 aperture is 80%, the aperture that qualified purified gas rinses variable valve 25 is 80%, the flow of qualified purified gas is 3500Nm
3/ h,
Step 2: enter qualified purified gas rinse stage, after qualified purified gas air inlet adjustment valve 11 described in above-mentioned steps one and qualified purified gas rinse variable valve 25 unlatching, model predictive controller 37 controls qualified purified gas flushing sequencing valve 28 by DCS main control card 38 and opens, the aperture that described qualified purified gas rinses sequencing valve 28 is 100%, qualified purified gas starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 430s;
Step 3: enter qualified purified gas empty stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps two, model predictive controller 37 controls qualified purified gas air inlet adjustment valve 11 by DCS main control card 38, qualified purified gas rinses variable valve 25 and qualified purified gas flushing sequencing valve 28 cuts out, open purge gas to give vent to anger sequencing valve 32 simultaneously, make qualified purified gas purge gas be sent to blowing-air recovery heat by emptying house steward 32;
Step 4: the adsorption tower 18 in the adsorption tower unit in above-mentioned adsorbent reactivation stage enters absorption phase, open unstripped gas sequencing valve 30 and qualified purified gas to give vent to anger sequencing valve 19, unstripped gas enters in the adsorption tower unit of above-mentioned absorption phase by unstripped gas sequencing valve 30, after adsorption tower 18 adsorbs, qualified purified gas enters qualified purified gas air intake opening 9 by qualified purified gas sequencing valve 19 and qualified purified gas components analysis instrument 24 of giving vent to anger of giving vent to anger, and now qualified purified gas components analysis instrument 24 of giving vent to anger carries out gas analysis to qualified purified gas;
Step 5: when the components analysis instrument 24 of giving vent to anger of the qualified purified gas described in above-mentioned steps four carries out gas analysis to qualified purified gas, when wherein carbon dioxide content is less than 1.5%, after the adsorption tower 18 entered described in step 4 in the adsorption tower unit of absorption phase enters the adsorbent reactivation stage, the step one, step 2 and the step 3 that adopt qualified purified gas to rinse in renovation process carry out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage.
The utility model adopts qualified purified gas flushing renovation process to regenerate adsorption tower unit adsorbent reactivation, comprises the steps:
Step one: qualified purified gas rinses the preparatory stage, when qualified purified gas air inlet pressure sensor 10 detects that Hydrogen Vapor Pressure is between 0.2 ~ 0.4MPa, qualified purified gas air inlet pressure sensor 10 will detect that qualified purified gas pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls qualified purified gas air inlet adjustment valve 11 by DCS main control card 38 and qualified purified gas flushing variable valve 25 is opened, described qualified purified gas air inlet adjustment valve 11 aperture is 80%, the aperture that qualified purified gas rinses variable valve 25 is 80%, the flow of qualified purified gas is 3500Nm
3/ h,
Step 2: enter qualified purified gas rinse stage, after qualified purified gas air inlet adjustment valve 11 described in above-mentioned steps one and qualified purified gas rinse variable valve 25 unlatching, model predictive controller 37 controls qualified purified gas flushing sequencing valve 28 by DCS main control card 38 and opens, the aperture that described qualified purified gas rinses sequencing valve 28 is 100%, qualified purified gas starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 430s;
Step 3: enter qualified purified gas empty stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps two, model predictive controller 37 controls qualified purified gas air inlet adjustment valve 11 by DCS main control card 38, qualified purified gas rinses variable valve 25 and qualified purified gas flushing sequencing valve 28 cuts out, open purge gas to give vent to anger sequencing valve 32 simultaneously, make qualified purified gas purge gas be sent to blowing-air recovery heat by emptying house steward 32;
Step 4: the adsorption tower 18 in the adsorption tower unit in above-mentioned adsorbent reactivation stage enters absorption phase, open unstripped gas sequencing valve 30 and qualified purified gas to give vent to anger sequencing valve 19, unstripped gas enters in the adsorption tower unit of above-mentioned absorption phase by unstripped gas sequencing valve 30, after adsorption tower 18 adsorbs, qualified purified gas enters qualified purified gas air intake opening 9 by qualified purified gas sequencing valve 19 and qualified purified gas components analysis instrument 24 of giving vent to anger of giving vent to anger, and now qualified purified gas components analysis instrument 24 of giving vent to anger carries out gas analysis to qualified purified gas;
Step 5: when the components analysis instrument 24 of giving vent to anger of the qualified purified gas described in above-mentioned steps four carries out gas analysis to qualified purified gas, when wherein carbon dioxide content is not less than 1.5%, after the adsorption tower 18 entered described in step 4 in the adsorption tower unit of absorption phase enters the adsorbent reactivation stage, when qualified purified gas air inlet pressure sensor 10 detects that Hydrogen Vapor Pressure is between 0.2 ~ 0.4MPa, qualified purified gas air inlet pressure sensor 10 will detect that qualified purified gas pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls qualified purified gas air inlet adjustment valve 11 by DCS main control card 38 and qualified purified gas flushing variable valve 25 is opened, described qualified purified gas air inlet adjustment valve 11 aperture is 80%, the aperture that qualified purified gas rinses variable valve 25 is 80%, the flow of qualified purified gas is 3500Nm
3/ h,
Step 6: qualified purified gas rinse stage again, after qualified purified gas air inlet adjustment valve 11 described in above-mentioned steps seven and qualified purified gas rinse variable valve 25 unlatching, model predictive controller 37 controls qualified purified gas flushing sequencing valve 28 by DCS main control card 38 and opens, the aperture that described qualified purified gas rinses sequencing valve 28 is 100%, qualified purified gas starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 350s;
Step 7: enter again qualified purified gas empty stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps six, analysis data are fed back to model predictive controller 37 by DCS database 39 and DCS main control card 38 by qualified purified gas components analysis instrument 24 of giving vent to anger, model predictive controller 37 controls qualified purified gas air inlet adjustment valve 11 by DCS main control card 38, qualified purified gas rinses variable valve 25 and qualified purified gas flushing sequencing valve 28 cuts out, make vacuum pump 36 open and open exhaust sequencing valve 35 simultaneously, evacuation processes is carried out to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, the hydrogen purge gas of evacuation processes is sent to blowing-air recovery heat by emptying house steward 32, the time of described evacuation processes is: 50s.
The utility model adopts mixing flushing renovation process to regenerate adsorption tower unit adsorbent reactivation, comprises the steps:
Step one: the preparatory stage is rinsed in mixing, when nitrogen air inlet pressure sensor 2 detects that nitrogen pressure is between 0.2 ~ 0.4MPa, nitrogen air inlet pressure sensor 2 will detect that nitrogen pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, and model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38 and nitrogen wash variable valve 14 is opened; Described nitrogen air inlet adjustment valve 3 aperture is 80%, and nitrogen wash variable valve 14 aperture is 50%, and the flow of nitrogen is 2500Nm
3/ h; When hydrogen gas pressure transducer 6 detects that Hydrogen Vapor Pressure is between 0.2 ~ 0.4MPa, hydrogen gas pressure transducer 6 will detect that Hydrogen Vapor Pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38 and hydrogen flushing variable valve 20 is opened, described hydrogen gas variable valve 7 aperture is 80%, the aperture that hydrogen rinses variable valve 20 is 20%, and the flow of hydrogen is 650Nm
3/ h;
Step 2: enter the nitrogen wash stage, after the valve of nitrogen air inlet adjustment described in above-mentioned steps one 3 and nitrogen wash variable valve 14 are opened, model predictive controller 37 controls nitrogen wash sequencing valve 17 by DCS main control card 38 and opens, the aperture of described nitrogen wash sequencing valve 17 is 100%, nitrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 350s;
Step 3: enter the nitrogen purge stage, when rinsing after adsorbent terminates described in above-mentioned steps two, model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38, nitrogen wash variable valve 14 and nitrogen wash sequencing valve 17 are closed, open purge gas to give vent to anger sequencing valve 32 simultaneously, make nitrogen wash gas be sent to blowing-air recovery heat by emptying house steward 32, the nitrogen wash stage terminates;
Step 4: enter hydrogen rinse stage, after hydrogen gas variable valve 7 described in above-mentioned steps one and hydrogen rinse variable valve 20 unlatching, model predictive controller 37 controls hydrogen flushing sequencing valve 23 by DCS main control card 38 and opens, the aperture that described hydrogen rinses sequencing valve 23 is 100%, hydrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 70s;
Step 5: enter empty stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps two, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38, hydrogen rinses variable valve 20 and hydrogen flushing sequencing valve 23 cuts out, open purge gas to give vent to anger sequencing valve 32 simultaneously, make hydrogen purge gas be sent to blowing-air recovery heat by emptying house steward 32, mixing is rinsed renovation process and is terminated;
Step 6: the adsorption tower 18 in the adsorption tower unit in above-mentioned adsorbent reactivation stage enters absorption phase, open unstripped gas sequencing valve 30 and qualified purified gas to give vent to anger sequencing valve 19, unstripped gas enters in the adsorption tower unit of above-mentioned absorption phase by unstripped gas sequencing valve 30, after adsorption tower 18 adsorbs, qualified purified gas enters qualified purified gas air intake opening 9 by qualified purified gas sequencing valve 19 and qualified purified gas components analysis instrument 24 of giving vent to anger of giving vent to anger, and now qualified purified gas components analysis instrument 24 of giving vent to anger carries out gas analysis to qualified purified gas;
Step 7: when the components analysis instrument 24 of giving vent to anger of the qualified purified gas described in above-mentioned steps six carries out gas analysis to qualified purified gas, when wherein carbon dioxide content is less than 1.5%, after the adsorption tower 18 entered described in step 6 in the adsorption tower unit of absorption phase enters the adsorbent reactivation stage, the step one of mixing flushing renovation process, step 2, step 3, step 4 and step 5 is adopted to carry out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage.
The utility model adopts mixing flushing renovation process to regenerate adsorption tower unit adsorbent reactivation, comprises the steps:
Step one: the preparatory stage is rinsed in mixing, when nitrogen air inlet pressure sensor 2 detects that nitrogen pressure is between 0.2 ~ 0.4MPa, nitrogen air inlet pressure sensor 2 will detect that nitrogen pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, and model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38 and nitrogen wash variable valve 14 is opened; Described nitrogen air inlet adjustment valve 3 aperture is 80%, and nitrogen wash variable valve 14 aperture is 50%, and the flow of nitrogen is 2500Nm
3/ h; When hydrogen gas pressure transducer 6 detects that Hydrogen Vapor Pressure is between 0.2 ~ 0.4MPa, hydrogen gas pressure transducer 6 will detect that Hydrogen Vapor Pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38 and hydrogen flushing variable valve 20 is opened, described hydrogen gas variable valve 7 aperture is 80%, the aperture that hydrogen rinses variable valve 20 is 20%, and the flow of hydrogen is 650Nm
3/ h;
Step 2: enter the nitrogen wash stage, after the valve of nitrogen air inlet adjustment described in above-mentioned steps one 3 and nitrogen wash variable valve 14 are opened, model predictive controller 37 controls nitrogen wash sequencing valve 17 by DCS main control card 38 and opens, the aperture of described nitrogen wash sequencing valve 17 is 100%, nitrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 350s;
Step 3: enter the nitrogen purge stage, when rinsing after adsorbent terminates described in above-mentioned steps two, model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38, nitrogen wash variable valve 14 and nitrogen wash sequencing valve 17 are closed, open purge gas to give vent to anger sequencing valve 32 simultaneously, make nitrogen wash gas be sent to blowing-air recovery heat by emptying house steward 32, the nitrogen wash stage terminates;
Step 4: enter hydrogen rinse stage, after hydrogen gas variable valve 7 described in above-mentioned steps one and hydrogen rinse variable valve 20 unlatching, model predictive controller 37 controls hydrogen flushing sequencing valve 23 by DCS main control card 38 and opens, the aperture that described hydrogen rinses sequencing valve 23 is 100%, hydrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 70s;
Step 5: enter empty stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps two, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38, hydrogen rinses variable valve 20 and hydrogen flushing sequencing valve 23 cuts out, open purge gas to give vent to anger sequencing valve 32 simultaneously, make hydrogen purge gas be sent to blowing-air recovery heat by emptying house steward 32, mixing is rinsed renovation process and is terminated;
Step 6: the adsorption tower 18 in the adsorption tower unit in above-mentioned adsorbent reactivation stage enters absorption phase, open unstripped gas sequencing valve 30 and qualified purified gas to give vent to anger sequencing valve 19, unstripped gas enters in the adsorption tower unit of above-mentioned absorption phase by unstripped gas sequencing valve 30, after adsorption tower 18 adsorbs, qualified purified gas enters qualified purified gas air intake opening 9 by qualified purified gas sequencing valve 19 and qualified purified gas components analysis instrument 24 of giving vent to anger of giving vent to anger, and now qualified purified gas components analysis instrument 24 of giving vent to anger carries out gas analysis to qualified purified gas;
Step 7: when the components analysis instrument 24 of giving vent to anger of the qualified purified gas described in above-mentioned steps six carries out gas analysis to qualified purified gas, when wherein carbon dioxide content is not less than 1.5%, after the adsorption tower 18 in the adsorption tower unit entering absorption phase described in step 6 enters regeneration stage, when nitrogen air inlet pressure sensor 2 detects that nitrogen pressure is between 0.2 ~ 0.4MPa, nitrogen air inlet pressure sensor 2 will detect that nitrogen pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38 and nitrogen wash variable valve 14 is opened, described nitrogen air inlet adjustment valve 3 aperture is 80%, and nitrogen wash variable valve 14 aperture is 50%, and the flow of nitrogen is 2500Nm
3/ h, when hydrogen gas pressure transducer 6 detects that Hydrogen Vapor Pressure is between 0.2 ~ 0.4MPa, hydrogen gas pressure transducer 6 will detect that Hydrogen Vapor Pressure feeds back to model predictive controller 37 by DCS database 39 and DCS main control card 38, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38 and hydrogen flushing variable valve 20 is opened, described hydrogen gas variable valve 7 aperture is 80%, the aperture that hydrogen rinses variable valve 20 is 20%, and the flow of hydrogen is 650Nm
3/ h,
Step 8: enter again the nitrogen wash stage, after the valve of nitrogen air inlet adjustment described in above-mentioned steps seven 3 and nitrogen wash variable valve 14 are opened, model predictive controller 37 controls nitrogen wash sequencing valve 17 by DCS main control card 38 and opens, the aperture of described nitrogen wash sequencing valve 17 is 100%, nitrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 350s;
Step 9: enter nitrogen empty stage again, when rinsing after adsorbent reactivation terminates described in above-mentioned steps eight, model predictive controller 37 controls nitrogen air inlet adjustment valve 3 by DCS main control card 38, nitrogen wash variable valve 14 and nitrogen wash sequencing valve 17 are closed, open purge gas to give vent to anger sequencing valve 32 simultaneously, make nitrogen wash gas be sent to blowing-air recovery heat by emptying house steward 32, the nitrogen wash stage terminates;
Step 10: enter hydrogen rinse stage again, after hydrogen gas variable valve 7 described in above-mentioned steps seven and hydrogen rinse variable valve 20 unlatching, model predictive controller 37 controls hydrogen flushing sequencing valve 23 by DCS main control card 38 and opens, the aperture that described hydrogen rinses sequencing valve 23 is 100%, hydrogen starts to rinse adsorbent and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, and its flushing adsorbent duration is: 70s;
Step 11: enter hydrogen empty stage, when rinsing after adsorbent reactivation terminates described in above-mentioned steps ten, analysis data are fed back to model predictive controller 37 by DCS database 39 and DCS main control card 38 by qualified purified gas components analysis instrument 24 of giving vent to anger, model predictive controller 37 controls hydrogen gas variable valve 7 by DCS main control card 38, hydrogen rinses variable valve 20 and hydrogen flushing sequencing valve 23 cuts out, make vacuum pump 36 open and open exhaust sequencing valve 35 simultaneously, evacuation processes is carried out to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, the hydrogen purge gas of evacuation processes is sent to blowing-air recovery heat by emptying house steward 32, the time of described evacuation processes is: 50s.
The utility model employing vacuumizes method of reproduction and regenerates adsorption tower unit adsorbent reactivation, comprises the steps:
Step one: vacuumize the method for reproduction preparatory stage, model predictive controller 37 controls vacuum pump 36 by DCS main control card 38 and opens, open exhaust sequencing valve 35 simultaneously, process is vacuumized to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage, be evacuated to adsorption column pressure sensor 13 and detect vacuum tightness when reaching-63Ka, vacuumize end; The air vacuumizing process is sent to blowing-air recovery heat by emptying house steward 32;
Step 2: adsorption column pressure sensor 13 described in above-mentioned steps one is detected vacuum tightness when reaching-63Ka, model predictive controller 37 is fed back to by DCS database 39 and DCS main control card 38, it is out of service that model predictive controller 37 controls vacuum pump 36 by DCS main control card 38, exhaust sequencing valve 35 cuts out, and vacuumizes method of reproduction and carries out adsorbent reactivation to the adsorption tower 18 in the adsorption tower unit in adsorbent reactivation stage and terminate.
A series of detailed description listed is above only illustrating for feasibility embodiment of the present utility model; they are also not used to limit protection domain of the present utility model, all do not depart from the utility model skill equivalent implementations of doing of spirit or change all should be included within protection domain of the present utility model.
Claims (2)
1. a pressure-variable adsorption agent regenerating control device, this regenerating control device comprises multimedium admission gear, flusher, emptier and control system, it is characterized in that:
A, multimedium admission gear comprise nitrogen inlet (1), hydrogen inlet (5) and qualified purified gas air intake opening (9), nitrogen inlet (1) by pipeline successively with nitrogen air inlet pressure sensor (2), nitrogen buffer tank (4) import on nitrogen air inlet adjustment valve (3) and flusher is connected, hydrogen inlet (5) by pipeline successively with hydrogen gas pressure transducer (6), hydrogen gas buffer (8) import on hydrogen gas variable valve (7) and flusher is connected, qualified purified gas air intake opening (9) by pipeline successively with qualified purified gas air inlet pressure sensor (10), qualified purified gas surge tank (12) import on qualified purified gas air inlet adjustment valve (11) and flusher is connected,
B, flusher comprise nitrogen buffer tank (4), hydrogen gas buffer (8) and qualified purified gas surge tank (12), nitrogen buffer tank (4) outlet by pipeline successively with nitrogen wash variable valve (14), nitrogen flow meter (15) is connected with nitrogen pressure sensor (16), nitrogen pressure sensor (16) is connected with the nitrogen wash sequencing valve (17) that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged respectively, hydrogen gas buffer (8) outlet rinses variable valve (20) with hydrogen successively by pipeline, hydrogen flowmeter (21) and hydrogen gas pressure sensor (22), hydrogen gas pressure sensor (22) rinses sequencing valve (23) with the hydrogen that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged respectively and is connected, qualified purified gas surge tank (12) outlet rinses variable valve (25) with qualified purified gas successively by pipeline, qualified purifying gas flow gauge (26) and qualified purified gas pressure transducer (27), qualified purified gas pressure transducer (27) is rinsed sequencing valve (28) with the qualified purified gas that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged respectively and is connected, the qualified purified gas that at least two group adsorption tower unit adsorbent reactivation stage air intake openings are arranged sequencing valve (19) components analysis instrument (24) of giving vent to anger with qualified purified gas respectively of giving vent to anger is connected, described qualified purified gas components analysis instrument (24) of giving vent to anger is connected with qualified purified gas air intake opening (9) by pipeline, described at least two group adsorption tower unit adsorbent reactivation stage gas outlets are provided with unstripped gas sequencing valve (30) be connected with raw material gas inlet (29) respectively, at least two group adsorption tower unit adsorbent reactivation stage gas outlets are provided with the first threeway (40) respectively and between corresponding unstripped gas sequencing valve (30), 3rd end of the first threeway (40) is connected with the emptying house steward (33) in emptier by purge gas sequencing valve (32) of giving vent to anger, 3rd end of the first threeway (40) and purge gas are given vent to anger between sequencing valve (32) and are provided with the second threeway (34), 3rd end of the second threeway (34) is connected with the vacuum pump (36) in emptier by exhaust sequencing valve (35), described qualified purified gas air intake opening (9) uses workshop section to be connected with back segment purified gas, at least be provided with an adsorption tower (18) respectively in described at least two group adsorption tower unit, described adsorption tower (18) is provided with adsorption column pressure sensor (13),
C, emptier comprise and are located at vacuum pump (36) and emptying house steward (33), and described vacuum pump (36) is connected by pipeline with emptying house steward (33);
D, control system comprises model predictive controller (37), DCS main control card (38) and DCS database (39), described nitrogen air inlet pressure sensor (2), hydrogen gas pressure transducer (6), qualified purified gas air inlet pressure sensor (10), nitrogen flow meter (15), nitrogen pressure sensor (16), hydrogen flowmeter (21), hydrogen gas pressure sensor (22), qualified purifying gas flow gauge (26), qualified purified gas pressure transducer (27), adsorption column pressure sensor (13) and qualified purified gas components analysis instrument (24) of giving vent to anger is connected with DCS database (39) respectively by data line, DCS database (39) is connected with model predictive controller (37) by DCS main control card (38), and model predictive controller (37) controls nitrogen air inlet adjustment valve (3) by DCS main control card (38), hydrogen gas variable valve (7), qualified purified gas air inlet adjustment valve (11), nitrogen wash variable valve (14), nitrogen wash sequencing valve (17), hydrogen rinses variable valve (20), hydrogen rinses sequencing valve (23), qualified purified gas rinses variable valve (25), qualified purified gas rinses sequencing valve (28), purge gas is given vent to anger sequencing valve (32), vacuum pump (36) and exhaust sequencing valve (35).
2. pressure-variable adsorption agent regenerating control device according to claim 1, is characterized in that: described often group between adsorption tower unit adopts mode in parallel to be connected.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520032944.7U CN204576212U (en) | 2015-01-19 | 2015-01-19 | Pressure-variable adsorption agent regenerating control device |
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| CN201520032944.7U CN204576212U (en) | 2015-01-19 | 2015-01-19 | Pressure-variable adsorption agent regenerating control device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104656618A (en) * | 2015-01-19 | 2015-05-27 | 河南心连心化肥有限公司 | Pressure-swing adsorbent regeneration control device and control method thereof |
| CN108176389A (en) * | 2018-01-17 | 2018-06-19 | 国网安徽省电力有限公司电力科学研究院 | SF6The adsorbent on-line regeneration method of purifying processing device |
-
2015
- 2015-01-19 CN CN201520032944.7U patent/CN204576212U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104656618A (en) * | 2015-01-19 | 2015-05-27 | 河南心连心化肥有限公司 | Pressure-swing adsorbent regeneration control device and control method thereof |
| CN104656618B (en) * | 2015-01-19 | 2017-05-31 | 河南心连心化肥有限公司 | Pressure-variable adsorption agent regenerating control device and its control method |
| CN108176389A (en) * | 2018-01-17 | 2018-06-19 | 国网安徽省电力有限公司电力科学研究院 | SF6The adsorbent on-line regeneration method of purifying processing device |
| CN108176389B (en) * | 2018-01-17 | 2020-09-01 | 国网安徽省电力有限公司电力科学研究院 | SF6Method for on-line regeneration of adsorbent in purification treatment apparatus |
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