CN1821057A - Method for oxygen enriching by improved two stage pressure swing adsorption - Google Patents
Method for oxygen enriching by improved two stage pressure swing adsorption Download PDFInfo
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Abstract
The improved two-stage pressure swing adsorption process features that oxygen and/or nitrogen are produced through separating air. The process is completed inside serial two-stage pressure swing adsorption apparatus, including the first stage of pressure swing adsorption apparatus for eliminate CO2, water and partial N2 and concentrating N2, and the second stage of pressure swing adsorption apparatus for eliminating N2 from the intermediate gas from the first stage and raising oxygen concentration. The first stage of pressure swing adsorption apparatus has the cycle in the adsorption tower comprising the steps of adsorption, replacement, vacuum pumping, reverse second section gas pressure raising, replaced gas pressure raising, ultimate pressure raising and pressure swing adsorption; and the second stage of pressure swing adsorption apparatus has the cycle in the adsorption tower comprising the steps of adsorption, reverse pressure lowering, and ultimate pressure raising and pressure swing adsorption.
Description
Technical field
The application is the applying date: on June 11st, 2004, and application number: 200410046596.5, denomination of invention: the dividing an application of a kind of application for a patent for invention of improved two sections transformations absorption method for oxygen enriching.The present invention relates to adopt two-stage pressure swing adsorption from air, to produce the method for oxygen enrichment.
Background technology
The present invention is the further improvement of two-stage pressure swing adsorption being produced oxygen enrichment patented technology (patent publication No. is CN1386565A) from air, also produce simultaneously and carry dense nitrogen, improve the rate of recovery of oxygen and nitrogen, the power consumption of whole oxygenerator and investment are further reduced.
Summary of the invention
Purpose of the present invention just provides a kind of improved two sections transformations absorption method for oxygen enriching, and this method has overcome the problems referred to above of prior art, compared with prior art saves power consumption and investment significantly, improves the oxygen recovery rate of whole device.
The objective of the invention is to implement like this.
The present invention adopts two-stage pressure swing adsorption separation of nitrogen and oxygen from air, product can be an oxygen, also can be nitrogen, can also be oxygen and nitrogen simultaneously, this method adopts two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus is used to remove carbonic acid gas, water and part nitrogen are also carried nitrogen dense, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration, the adsorption tower of first stage pressure swing adsorption apparatus experience absorption A successively in a loop cycle, displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions are to boost pressure 2ER, the displacement gas R ' that boosts, the FR pressure swing adsorption technique step of finally boosting; The adsorption tower of second stage pressure swing adsorption apparatus experience absorption A, reverse drop pressure BD ', the final FR pressure swing adsorption technique step of boosting successively in a loop cycle.
After absorption A processing step, increase forward drop pressure ED processing step at the second stage pressure swing adsorption apparatus adsorption tower, increase the reverse ER of boosting processing step simultaneously after reverse drop pressure BD ' processing step is finished, the gas mixture of the ER processing step that boosts is from step-down ED processing step.
The first stage pressure swing adsorption apparatus adsorption tower increases two ends drop pressure 2ED ' processing step after absorption A processing step, simultaneously increase boost pressure 2ER ' processing step two sections circulation of vital energy in the wrong directions after boost pressure 2ER processing step is finished, the gas mixture of two ends boost pressure 2ER ' processing step is from drop pressure 2ED ' processing step.
The first stage pressure swing adsorption apparatus adsorption tower increases reverse step-down BD processing step after displacement P ' processing step.
The gas mixture that the reverse drop pressure BD ' processing step of the second stage pressure swing adsorption apparatus adsorption tower is emitted enters surge tank V1, till pressure equilibrium, the first stage pressure swing adsorption apparatus adsorption tower is when carrying out two sections circulation of vital energy in the wrong directions to boost pressure 2ER processing step simultaneously, adsorption tower is communicated with surge tank V1, till pressure equilibrium.
The mean concns of oxygen was greater than 21～80% (V) during the first stage pressure swing adsorption apparatus adsorption tower adsorption step was worked off one's feeling vent one's spleen.
The mean concns of oxygen was greater than 21～25% (V) during the first stage pressure swing adsorption apparatus adsorption tower adsorption step was worked off one's feeling vent one's spleen.
The pressure of two-stage pressure swing adsorption apparatus adsorption step A is 0.001～0.1MPa (gauge pressure).
The sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is activated alumina and molecular sieve; The sorbent material of filling only is a molecular sieve in the second stage pressure swing adsorption apparatus adsorption tower.
The reverse drop pressure ED ' of the second stage pressure swing adsorption apparatus adsorption tower and two sections circulation of vital energy in the wrong directions of the first stage pressure swing adsorption apparatus adsorption tower to the number of times of boost pressure 2ER more than or equal to 1.
The reverse drop pressure ED ' of the second stage pressure swing adsorption apparatus adsorption tower and two sections circulation of vital energy in the wrong directions of the first stage pressure swing adsorption apparatus adsorption tower are 3～7 times to the number of times of boost pressure 2ER.
The present invention is used for from air separation of nitrogen and oxygen, product can be an oxygen, also can be nitrogen, can also be oxygen and nitrogen simultaneously, this method adopts two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus is used to remove carbonic acid gas, water and part nitrogen are also carried nitrogen dense, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration, the adsorption tower of first stage pressure swing adsorption apparatus experience absorption A successively in a loop cycle, two ends drop pressure 2ED ', displacement P ', reverse step-down BD, two sections circulation of vital energy in the wrong directions are to boost pressure 2ER, two ends boost pressure 2ER ', the displacement gas R ' that boosts, the FR pressure swing adsorption technique step of finally boosting; The second stage pressure swing adsorption apparatus adsorption tower experience absorption A, forward drop pressure ED, reverse drop pressure BD ', reverse boost pressure ER, the final FR pressure swing adsorption technique step of boosting successively in a loop cycle.
The pressure of two-stage pressure swing adsorption apparatus adsorption step A is 0.3～0.6MPa gauge pressure.
The present invention is used for from air separation of nitrogen and oxygen, product can be an oxygen, also can be nitrogen, can also be oxygen and nitrogen simultaneously, this method adopts two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus is used to remove carbonic acid gas, water and part nitrogen are also carried nitrogen dense, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration, the adsorption tower of first stage pressure swing adsorption apparatus experience absorption A successively in a loop cycle, two ends drop pressure 2ED ', vacuumize VC, two sections circulation of vital energy in the wrong directions are to boost pressure 2ER, two ends boost pressure 2ER ', the FR pressure swing adsorption technique step of finally boosting; The adsorption tower of second stage pressure swing adsorption apparatus experience absorption A, reverse drop pressure BD ', the final FR pressure swing adsorption technique step of boosting successively in a loop cycle.The first stage pressure swing adsorption apparatus adsorption tower increases reverse step-down BD processing step after the drop pressure 2ED ' processing step of two ends.
Description of drawings
Fig. 1 is the processing step working procedure table of embodiment first stage pressure swing adsorption apparatus.
Fig. 2 is the processing step working procedure table of embodiment second stage pressure swing adsorption apparatus.
Fig. 3 is the process flow sheet of embodiment 1.
Embodiment
Unstripped gas of the present invention is an air, its typical table composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
The present invention adopts two-stage pressure swing adsorption to produce oxygen enrichment from air, this method adopts two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus is used to remove vaporous water, carbonic acid gas and part nitrogen, the mean concns of oxygen was 21～80% (V) during the adsorption tower adsorption step was worked off one's feeling vent one's spleen, and the sorbent material that loads from down to up in the adsorption tower is activated alumina and molecular sieve; Second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration, and the sorbent material of filling is a molecular sieve in the adsorption tower.The pressure of two-stage pressure swing adsorption apparatus adsorption step A is 0.001～0.1MPa (gauge pressure).Each adsorption tower of two-stage pressure swing adsorption apparatus experiences following steps successively in a circulation.
First stage pressure swing adsorption apparatus:
(1) absorption A
Air is sent into the adsorption tower opening for feed that is in adsorption step, sorbent material in the adsorption tower is components such as water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, the components such as argon gas of Xi Fu part nitrogen and difficult absorption do not flow out from exit end and enter the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, As time goes on, the total amount of components such as adsorbent water, carbonic acid gas and part nitrogen constantly increases, when the adsorbents adsorb said components is saturated, stop air inlet, this moment, absorption finished.
(2) two ends drop pressure 2ED '
After absorption finishes, in the adsorption tower in the dead space gas oxygen concentration higher, this part oxygen need be recycled, for this reason, the gas in the adsorption tower from two ends step-down up and down.Dead space gas import and export to be discharged from adsorption tower and is entered this section and finished two sections circulation of vital energy in the wrong directions and carry out the two ends 2ER ' that boosts to the corresponding adsorption tower of boost pressure 2ER step.Two ends drop pressure 2ED ' number of times can be (as 1～3 time) more than 1 time or 1 time.
After absorption finishes, can also be only forward drop pressure or reverse drop pressure.
(3) displacement P '
After two ends drop pressure 2ED ' step finishes, enter from the bottom of adsorption tower with first section gas that vacuumizes the VC step replacement of oxygen residual in the tower is gone out, the gas mixture that cements out from adsorption tower enters this section and has finished two sections circulation of vital energy in the wrong directions and carry out the substitution gas R ' that boosts to the corresponding adsorption tower of boost pressure 2ER step or two ends boost pressure 2ER ' step.
(4) the contrary BD of putting
After the displacement P ' end, that this part gas is reverse from adsorption tower bottom emptying or as product.
(5) vacuumize VC
After displacement P ' ends, from the adsorption tower bottom with vacuum pump with the emptying of releasing of adsorbent water, carbonic acid gas and nitrogen, make sorbent material obtain regenerating.
(6) two sections circulation of vital energy in the wrong directions are to boost pressure 2ER
Vacuumize after VC finishes, utilize the absorption of the second stage pressure swing adsorption apparatus adsorption tower to finish or the gas after forward drop pressure ED finishes enters this section and finished the adsorption tower that vacuumizes the VC step, adsorption tower is boosted.Two sections circulation of vital energy in the wrong directions can be (as 1～7 time) more than 1 time or 1 time to 2ER number of boost pressure.
(7) two ends boost pressure 2ER '
Two sections circulation of vital energy in the wrong directions are utilized this section two ends drop pressure 2ED ' step expellant gas after boost pressure 2ER finishes, enter adsorption tower from entrance end, make the adsorption tower pressure that progressively raises, and two ends boost pressure 2ER ' equates with the number of times of two ends drop pressure 2ED '.The gas of each two ends boost pressure 2ER ' is from the two ends drop pressure 2ED ' gas of different adsorption towers.This section adsorption tower two ends boost pressure 2ER ' step and common boost pressure ER step are different, common adsorption tower boost pressure ER step gas is that the exit end from adsorption tower enters, and enters and this section adsorption tower two ends boost pressure 2ER ' step gas is import and export two ends from adsorption tower.
(8) the displacement gas R ' that boosts
Two ends boost pressure 2ER ' or two sections circulation of vital energy in the wrong directions are after boost pressure 2ER finishes, and the adsorption tower exit gas that is in displacement P ' step with this section boosts.
(9) FR that finally boosts
Displacement gas boosts after the R ' end, utilizes the adsorption tower that is in adsorption step to work off one's feeling vent one's spleen and from the top adsorption tower is boosted, and until being raised to adsorptive pressure, also can utilize raw air that adsorption tower is raised to adsorptive pressure.
Second stage pressure swing adsorption apparatus
(1) absorption A
The adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step is worked off one's feeling vent one's spleen and is sent into the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, sorbent material in the adsorption tower optionally adsorbs nitrogen, and components such as the oxygen of difficult absorption and argon gas are discharged from exit end and entered oxygen enrichment surge tank or next workshop section.As time goes on, adsorbent nitrogen total amount constantly increases, and when adsorbents adsorb nitrogen is saturated, stops air inlet, and this moment, absorption finished, and oxygen concentration is controlled at the level of product requirement in working off one's feeling vent one's spleen.
(2) drop pressure ED forward
After absorption finished, dead space gas was discharged from the adsorption tower outlet and is entered this section and finished the corresponding adsorption tower of reverse drop pressure BD ' step and boost in the adsorption tower, and two pressure towers can equate, also can be unequal, meet the demands to guarantee the product oxygen-rich concentration.Forward ED number of drop pressure can be (as 1～3 time) more than 1 time or 1 time.
(3) reverse drop pressure BD '
Absorption or after forward drop pressure ED finishes is reversely directly carried out the two section circulation of vital energy in the wrong directions to boost pressure 2ER with the gas gradation in the tower to first section adsorption tower of having finished to vacuumize VC from the adsorption tower bottom.BD number of reverse drop pressure can be (as 1～7 time) more than 1 time or 1 time.。
Reverse when the gas gradation in the tower being carried out two sections circulation of vital energy in the wrong directions to boost pressure 2ER to first section adsorption tower of having finished to vacuumize VC from adsorption tower bottom, can also be with the first reverse surge tank of putting into of gas in the adsorption tower, and then the gas in the surge tank is sent into the adsorption tower that first stage pressure swing adsorption apparatus vacuumizes after VC finishes carry out two sections circulation of vital energy in the wrong directions to boost pressure 2ER, the quantity of surge tank equates with the number of times of reverse drop pressure BD '.
(4) the reverse ER that boosts
Reverse drop pressure BD ' utilizes forward drop pressure ED step expellant gas after finishing, and enters adsorption tower from exit end, makes adsorption tower rising pressure.
(5) FR that finally boosts
The adsorption tower that utilization is in adsorption step is worked off one's feeling vent one's spleen and from the top adsorption tower is boosted, until being raised to adsorptive pressure.
Embodiments of the invention 1:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.01MPa (G)
As shown in Figure 3, adsorption tower A～D totally 4 form first stage pressure swing adsorption apparatus.The sorbent material that loads from down to up in the adsorption tower is followed successively by activated alumina and molecular sieve, moves single tower absorption and once all presses program, utilizes vacuum pipeline G15 that adsorption tower is vacuumized by vacuum pump P1; Adsorption tower a～d is totally 4 composition second stage pressure swing adsorption apparatus.The sorbent material of filling is a molecular sieve in the adsorption tower, moves single tower absorption and once all presses program.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.First section and second stage pressure swing adsorption apparatus also can adopt the adsorption tower more than four to make up.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER, displacement gas boost R ', the final FR pressure swing adsorption technique step of boosting; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experience absorption A, reverse drop pressure BD ', the final FR pressure swing adsorption technique step of boosting successively in a loop cycle.
Be example with the A tower now, contrast Fig. 1 and Fig. 3 illustrate the processing step of the present embodiment first stage pressure swing adsorption apparatus adsorption tower in a working cycle:
(1) absorption A
At this moment, the A tower has been finished the FR step of finally boosting, open sequencing valve 1A, 2A, air enters adsorption tower A through pipeline G11, in adsorption tower A, sorbent material is the water in the absorbed air successively optionally, components such as carbonic acid gas and part nitrogen, the components such as argon gas of Xi Fu part nitrogen and difficult absorption do not flow out from exit end and enter the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, As time goes on, adsorbent water, the total amount of components such as carbonic acid gas and part nitrogen constantly increases, when the adsorbents adsorb said components is saturated, stop air inlet, this moment, absorption finished, and closed sequencing valve 1A, 2A, nitrogen gas concn is controlled at 70～78% (V) in working off one's feeling vent one's spleen.
(2) displacement P '
After absorption finishes, open sequencing valve 6A, 4A and 4C, enter the C tower with vacuum pump outlet gas through pipeline G16 and G14 and the C tower is carried out displacement gas boost (abbreviation R '), after the nitrogen gas concn in the A tower meets the demands, close sequencing valve 6A, 4A and 4C.
(3) vacuumize VC
After displacement P ' ends, open sequencing valve 5A, from the adsorption tower bottom with vacuum pump with the release emptying or of adsorbent water, carbonic acid gas and nitrogen as product, make sorbent material obtain regenerating simultaneously.
(4) two sections circulation of vital energy in the wrong directions are to boost pressure 2ER
After vacuumizing the VC end, open sequencing valve 5a, 4A and KV8, utilize the gas of the reverse drop pressure BD ' step of the second stage pressure swing adsorption apparatus adsorption tower a to enter adsorption tower A, A boosts to adsorption tower.
(5) FR that finally boosts
Two sections circulation of vital energy in the wrong directions are opened sequencing valve KV6 and 3A after boost pressure 2ER finishes, utilize the adsorption tower that is in adsorption step to work off one's feeling vent one's spleen and boost from the top to the A tower, when the A pressure tower rises near adsorptive pressure, close sequencing valve KV6 and 3A.
So far, the A tower has been finished a circulation, can enter next circulation again.B～D adsorption tower is the same with the circulation step of A tower, just staggers mutually on the time, sees Fig. 1 and Fig. 3.
Be example with a tower now, contrast Fig. 2 and Fig. 3 illustrate the processing step of the present embodiment second stage pressure swing adsorption apparatus adsorption tower in a working cycle:
(1) absorption A
At this moment, the a tower has been finished the FR step of finally boosting, open sequencing valve 1a, 2a, middle gas mixture enters adsorption tower a through pipeline G21, in adsorption tower a, the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step is worked off one's feeling vent one's spleen and is sent into the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, and the sorbent material in the adsorption tower optionally adsorbs nitrogen, is difficult for components such as the oxygen of absorption and argon gas and discharges from exit end and enter oxygen enrichment surge tank or next workshop section.As time goes on, adsorbent nitrogen total amount constantly increases, and when adsorbents adsorb nitrogen is saturated, stops air inlet, and this moment, absorption finished, and closed sequencing valve 1a, 2a.
(2) reverse drop pressure BD '
Absorption is opened sequencing valve 5a, 4A and KV8 after finishing, and contrary the putting into into adsorption tower A of the gas in the adsorption tower a boosted.
(3) FR that finally boosts
Reverse drop pressure BD ' opens sequencing valve KV7 and 3a after finishing, and utilizes the adsorption tower that is in adsorption step to work off one's feeling vent one's spleen and boosts from the top to a tower, when a pressure tower rises near adsorptive pressure, closes sequencing valve KV7 and 3a.
So far, a tower has been finished a circulation, can enter next circulation again.B～h adsorption tower is the same with the circulation step of a tower, just staggers mutually on the time, sees Fig. 2 and Fig. 3.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 2:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.01MPa (G)
Adsorption tower A～G is totally 7 composition first stage pressure swing adsorption apparatus.The sorbent material that loads from down to up in the adsorption tower is followed successively by activated alumina and molecular sieve, moves the absorption of three towers and all presses program three times; Adsorption tower a～g is totally 7 composition second stage pressure swing adsorption apparatus, and the sorbent material of filling is a molecular sieve in the adsorption tower, moves the absorption of five towers and all presses program three times.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 3:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.01MPa (G)
Adsorption tower A～G is totally 7 composition first stage pressure swing adsorption apparatus.The sorbent material that loads from down to up in the adsorption tower is followed successively by activated alumina and molecular sieve, moves the absorption of three towers and all presses program three times; Adsorption tower a～g is totally 7 composition second stage pressure swing adsorption apparatus, and the sorbent material of filling is a molecular sieve in the adsorption tower, moves the absorption of four towers and all presses program three times.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, forward drop pressure ED, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, reverse boost pressure ER, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 4:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.02MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 5:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.02MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, forward drop pressure ED, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, reverse boost pressure ER, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 6:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.05MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 7:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.05MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', reverse step-down BD, vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 8:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.05MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, forward drop pressure ED, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, reverse boost pressure ER, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 9:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.05MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', reverse step-down BD, vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, forward drop pressure ED, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, reverse boost pressure ER, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 10:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.1MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', reverse step-down BD, vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, forward drop pressure ED, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, reverse boost pressure ER, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.9% (V), oxygen recovery rate is greater than 99% (V).
Embodiments of the invention 11:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.3MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experience absorption A successively in a loop cycle, two ends are drop pressure 2E1D ' for the first time, two ends are drop pressure 2E2D ' for the second time, two ends are drop pressure 2E3D ' for the third time, displacement P ', reverse step-down BD, vacuumize VC, two sections circulation of vital energy in the wrong directions are to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions are to the boost pressure 2ER2 second time, two sections circulation of vital energy in the wrong directions are to the boost pressure 2ER1 first time, two ends are boost pressure 2E3R ' for the third time, two ends are boost pressure 2E2R ' for the second time, two ends are boost pressure 2E1R ' for the first time, the displacement gas R ' that boosts, the FR pressure swing adsorption technique step of finally boosting; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experience absorption A successively in a loop cycle, drop pressure E1D for the first time forward, drop pressure E2D for the second time forward, drop pressure E3D for the third time forward, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the reverse E3R of boost pressure for the third time, reverse second time boost pressure E2R, reverse first time boost pressure E1R, the FR pressure swing adsorption technique step of finally boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.9% (V), oxygen recovery rate is greater than 99% (V).
Embodiments of the invention 12:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.3MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', reverse step-down BD, vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experience absorption A successively in a loop cycle, drop pressure E1D for the first time forward, drop pressure E2D for the second time forward, drop pressure E3D for the third time forward, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the reverse E3R of boost pressure for the third time, reverse second time boost pressure E2R, reverse first time boost pressure E1R, the FR pressure swing adsorption technique step of finally boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.9% (V), oxygen recovery rate is greater than 99% (V).
Embodiments of the invention 13:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.01MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experiences absorption A successively in a loop cycle, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the FR pressure swing adsorption technique step of finally boosting, the gas of the second stage pressure swing adsorption apparatus adsorption tower reverse first time of drop pressure B1D ' is put into surge tank V1 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V1 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse first time of boost pressure 2ER1 again; The gas of the second stage pressure swing adsorption apparatus adsorption tower reverse second time of drop pressure B2D ' is put into surge tank V2 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V2 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse second time of boost pressure 2ER2 again; The gas of the reverse drop pressure for the third time of second stage pressure swing adsorption apparatus adsorption tower B3D ' is put into surge tank V3 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V3 and the adsorption tower of the reverse boost pressure for the third time of first stage pressure swing adsorption apparatus adsorption tower 2ER3 again.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 14:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.01MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experiences absorption A successively in a loop cycle, drop pressure ED forward, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, reverse boost pressure ER, the FR pressure swing adsorption technique step of finally boosting, the gas of the second stage pressure swing adsorption apparatus adsorption tower reverse first time of drop pressure B1D ' is put into surge tank V1 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V1 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse first time of boost pressure 2ER1 again; The gas of the second stage pressure swing adsorption apparatus adsorption tower reverse second time of drop pressure B2D ' is put into surge tank V2 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V2 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse second time of boost pressure 2ER2 again; The gas of the reverse drop pressure for the third time of second stage pressure swing adsorption apparatus adsorption tower B3D ' is put into surge tank V3 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V3 and the adsorption tower of the reverse boost pressure for the third time of first stage pressure swing adsorption apparatus adsorption tower 2ER3 again.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 15:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.05MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experiences absorption A successively in a loop cycle, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the FR pressure swing adsorption technique step of finally boosting, the gas of the second stage pressure swing adsorption apparatus adsorption tower reverse first time of drop pressure B1D ' is put into surge tank V1 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V1 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse first time of boost pressure 2ER1 again; The gas of the second stage pressure swing adsorption apparatus adsorption tower reverse second time of drop pressure B2D ' is put into surge tank V2 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V2 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse second time of boost pressure 2ER2 again; The gas of the reverse drop pressure for the third time of second stage pressure swing adsorption apparatus adsorption tower B3D ' is put into surge tank V3 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V3 and the adsorption tower of the reverse boost pressure for the third time of first stage pressure swing adsorption apparatus adsorption tower 2ER3 again.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 16:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.05MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experiences absorption A successively in a loop cycle, drop pressure ED forward, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, reverse boost pressure ER, the FR pressure swing adsorption technique step of finally boosting, the gas of the second stage pressure swing adsorption apparatus adsorption tower reverse first time of drop pressure B1D ' is put into surge tank V1 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V1 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse first time of boost pressure 2ER1 again; The gas of the second stage pressure swing adsorption apparatus adsorption tower reverse second time of drop pressure B2D ' is put into surge tank V2 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V2 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse second time of boost pressure 2ER2 again; The gas of the reverse drop pressure for the third time of second stage pressure swing adsorption apparatus adsorption tower B3D ' is put into surge tank V3 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V3 and the adsorption tower of the reverse boost pressure for the third time of first stage pressure swing adsorption apparatus adsorption tower 2ER3 again.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 17:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 50% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.01MPa (G)
Adsorption tower A～G is totally 7 composition first stage pressure swing adsorption apparatus.The sorbent material that loads from down to up in the adsorption tower is followed successively by activated alumina and molecular sieve, moves the absorption of three towers and all presses program three times; Adsorption tower a～g is totally 7 composition second stage pressure swing adsorption apparatus, and the sorbent material of filling is a molecular sieve in the adsorption tower, moves the absorption of five towers and all presses program three times.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, the displacement gas first time; Oxygen concentration was controlled at about 50% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 50% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 18:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 50% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.01MPa (G)
Adsorption tower A～G is totally 7 composition first stage pressure swing adsorption apparatus.The sorbent material that loads from down to up in the adsorption tower is followed successively by activated alumina and molecular sieve, moves the absorption of three towers and all presses program three times; Adsorption tower a～g is totally 7 composition second stage pressure swing adsorption apparatus, and the sorbent material of filling is a molecular sieve in the adsorption tower, moves the absorption of four towers and all presses program three times.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, the displacement gas first time; Oxygen concentration was controlled at about 50% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, forward drop pressure ED, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, reverse boost pressure ER, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 50% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 19:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 50% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.05MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 50% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, forward drop pressure ED, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, reverse boost pressure ER, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 50% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5% (V).
Embodiments of the invention 20:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.6MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', reverse step-down BD, vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experience absorption A successively in a loop cycle, drop pressure E1D for the first time forward, drop pressure E2D for the second time forward, drop pressure E3D for the third time forward, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the reverse E3R of boost pressure for the third time, reverse second time boost pressure E2R, reverse first time boost pressure E1R, the FR pressure swing adsorption technique step of finally boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.9% (V), oxygen recovery rate is greater than 99% (V).
Embodiments of the invention 21:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.6MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', reverse step-down BD, vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experiences absorption A successively in a loop cycle, drop pressure E1D for the first time forward, drop pressure E2D for the second time forward, drop pressure E3D for the third time forward, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the reverse E3R of boost pressure for the third time, reverse second time boost pressure E2R, reverse first time boost pressure E1R, the FR pressure swing adsorption technique step of finally boosting, the gas of the second stage pressure swing adsorption apparatus adsorption tower reverse first time of drop pressure B1D ' is put into surge tank V1 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V1 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse first time of boost pressure 2ER1 again; The gas of the second stage pressure swing adsorption apparatus adsorption tower reverse second time of drop pressure B2D ' is put into surge tank V2 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V2 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse second time of boost pressure 2ER2 again; The gas of the reverse drop pressure for the third time of second stage pressure swing adsorption apparatus adsorption tower B3D ' is put into surge tank V3 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V3 and the adsorption tower of the reverse boost pressure for the third time of first stage pressure swing adsorption apparatus adsorption tower 2ER3 again.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.9% (V), oxygen recovery rate is greater than 99.6% (V).
Embodiments of the invention 22:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.6MPa (G)
The sorbent material that the sorbent material that loads from down to up in the first stage pressure swing adsorption apparatus adsorption tower is followed successively by filling in activated alumina and the molecular sieve second stage pressure swing adsorption apparatus adsorption tower is a molecular sieve.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', displacement P ', reverse step-down BD, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to boost R ', the final FR pressure swing adsorption technique step of boosting of boost pressure 2ER1, two ends boost pressure 2ER ', the displacement gas first time; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower experiences absorption A successively in a loop cycle, drop pressure E1D for the first time forward, drop pressure E2D for the second time forward, drop pressure E3D for the third time forward, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the reverse E3R of boost pressure for the third time, reverse second time boost pressure E2R, reverse first time boost pressure E1R, the FR pressure swing adsorption technique step of finally boosting, the gas of the second stage pressure swing adsorption apparatus adsorption tower reverse first time of drop pressure B1D ' is put into surge tank V1 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V1 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse first time of boost pressure 2ER1 again; The gas of the second stage pressure swing adsorption apparatus adsorption tower reverse second time of drop pressure B2D ' is put into surge tank V2 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V2 and the adsorption tower of the first stage pressure swing adsorption apparatus adsorption tower reverse second time of boost pressure 2ER2 again; The gas of the reverse drop pressure for the third time of second stage pressure swing adsorption apparatus adsorption tower B3D ' is put into surge tank V3 and is all pressed, and carries out pressure equilibrium with the gas of surge tank V3 and the adsorption tower of the reverse boost pressure for the third time of first stage pressure swing adsorption apparatus adsorption tower 2ER3 again.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.9% (V), oxygen recovery rate is greater than 99.6% (V).
Embodiments of the invention 23:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.01MPa (G)
Adsorption tower A～G is totally 7 composition first stage pressure swing adsorption apparatus.The sorbent material that loads from down to up in the adsorption tower is followed successively by activated alumina and molecular sieve, moves the absorption of three towers and all presses program three times; Adsorption tower a～g is totally 7 composition second stage pressure swing adsorption apparatus, and the sorbent material of filling is a molecular sieve in the adsorption tower, moves the absorption of five towers and all presses program three times.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to the first time boost pressure 2ER1, two ends boost pressure 2ER ', the final FR pressure swing adsorption technique step of boosting; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5%
Embodiments of the invention 24:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.1MPa (G)
Adsorption tower A～G is totally 7 composition first stage pressure swing adsorption apparatus.The sorbent material that loads from down to up in the adsorption tower is followed successively by activated alumina and molecular sieve, moves the absorption of three towers and all presses program three times; Adsorption tower a～g is totally 7 composition second stage pressure swing adsorption apparatus, and the sorbent material of filling is a molecular sieve in the adsorption tower, moves the absorption of five towers and all presses program three times.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', reverse step-down BD, vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to the first time boost pressure 2ER1, two ends boost pressure 2ER ', the final FR pressure swing adsorption technique step of boosting; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5%
Embodiments of the invention 25:
This routine unstripped gas is an air.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, and oxygen concentration was controlled at (being the product oxygen enrichment) about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen.
The air of present embodiment is composed as follows:
| Component | O 2 | N 2 | Ar | CO 2 | Other | ∑ |
| Concentration (%) (V) | 20.93 | 78.03 | 0.932 | 0.03 | 0.078 | 100 |
Temperature :≤45 ℃
Pressure: 0.01MPa (G)
Adsorption tower A～G is totally 7 composition first stage pressure swing adsorption apparatus.The sorbent material that loads from down to up in the adsorption tower is followed successively by activated alumina and molecular sieve, moves the absorption of three towers and all presses program three times; Adsorption tower a～g is totally 7 composition second stage pressure swing adsorption apparatus, and the sorbent material of filling is a molecular sieve in the adsorption tower, moves the absorption of five towers and all presses program three times.Present embodiment is with above-mentioned two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus removes airborne vaporous water, carbonic acid gas and part nitrogen, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration.
Air admission first stage pressure swing adsorption apparatus is in the adsorption tower of adsorption step, sorbent material in the adsorption tower is components such as vaporous water, carbonic acid gas and part nitrogen in the absorbed air successively optionally, components such as the oxygen of Xi Fu part nitrogen and difficult absorption and argon are not discharged from exit end and are entered the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step, molecular sieve in the adsorption tower property selected ground absorption nitrogen, components such as the oxygen of difficult absorption and argon are discharged from exit end and are entered product oxygen enrichment surge tank.Oxygen concentration was controlled at 21～23% (V) during the adsorption tower that first stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, two ends drop pressure 2ED ', vacuumize VC, two sections circulation of vital energy in the wrong directions to boost pressure 2ER3 for the third time, two sections circulation of vital energy in the wrong directions to the second time boost pressure 2ER2, two sections circulation of vital energy in the wrong directions to the first time boost pressure 2ER1, two ends boost pressure 2ER ', the final FR pressure swing adsorption technique step of boosting; Oxygen concentration was controlled at about 93% (V) during the adsorption tower that second stage pressure swing adsorption apparatus is in adsorption step was worked off one's feeling vent one's spleen, its adsorption tower in a loop cycle successively experience absorption A, forward drop pressure ED, reverse first time drop pressure B1D ', reverse second time drop pressure B2D ', the reverse B3D ' of drop pressure for the third time, reverse boost pressure ER, the final FR pressure swing adsorption technique step of boosting.
The present embodiment result be oxygen concentration greater than 93% (V), nitrogen gas concn is greater than 99.7% (V), oxygen recovery rate is greater than 98.5%.
Claims (5)
1, a kind of improved two sections transformations absorption method for oxygen enriching, it is characterized in that this method is used for from air separation of nitrogen and oxygen, product can be an oxygen, also can be nitrogen, can also be oxygen and nitrogen simultaneously, this method adopts two stage pressure swing adsorption apparatus serial operations, first stage pressure swing adsorption apparatus is used to remove carbonic acid gas, water and part nitrogen are also carried nitrogen dense, second stage pressure swing adsorption apparatus is used for the nitrogen of the effusive middle gas of the first stage pressure swing adsorption apparatus adsorption tower adsorption step is further removed, and oxygen is increased to required concentration, the adsorption tower of first stage pressure swing adsorption apparatus experience absorption A successively in a loop cycle, two ends drop pressure 2ED ', vacuumize VC, two sections circulation of vital energy in the wrong directions are to boost pressure 2ER, two ends boost pressure 2ER ', the FR pressure swing adsorption technique step of finally boosting; The adsorption tower of second stage pressure swing adsorption apparatus experience absorption A, reverse drop pressure BD ', the final FR pressure swing adsorption technique step of boosting successively in a loop cycle.
2, a kind of improved two sections transformations absorption method for oxygen enriching according to claim 1, it is characterized in that after absorption A processing step, increasing forward drop pressure ED processing step at the second stage pressure swing adsorption apparatus adsorption tower, increase the reverse ER of boosting processing step simultaneously after reverse drop pressure BD ' processing step is finished, the gas mixture of the ER processing step that boosts is from step-down ED processing step.
3, a kind of improved two sections transformations absorption method for oxygen enriching according to claim 1 and 2 is characterized in that the first stage pressure swing adsorption apparatus adsorption tower increases reverse step-down BD processing step after the drop pressure 2ED ' processing step of two ends.
4, a kind of improved two sections transformations absorption method for oxygen enriching according to claim 1 and 2, it is characterized in that the gas mixture that the reverse drop pressure BD ' processing step of the second stage pressure swing adsorption apparatus adsorption tower is emitted enters surge tank V1, till pressure equilibrium, the first stage pressure swing adsorption apparatus adsorption tower is when carrying out two sections circulation of vital energy in the wrong directions to boost pressure 2ER processing step simultaneously, adsorption tower is communicated with surge tank V1, till pressure equilibrium.
5, a kind of improved two sections transformations absorption method for oxygen enriching according to claim 1 and 2, the pressure that it is characterized in that two-stage pressure swing adsorption apparatus adsorption step A is 0.005～0.6MPa gauge pressure.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101952011A (en) * | 2007-12-12 | 2011-01-19 | Co2Crc技术股份有限公司 | A plant and process for recovering carbon dioxide |
| CN101549240B (en) * | 2009-04-23 | 2011-05-04 | 天津大学 | Method for absorbing methane in condensed coal bed gas through pressure varying mode including carbon dioxide replacement |
| CN109745828A (en) * | 2017-11-03 | 2019-05-14 | 中国科学院大连化学物理研究所 | A kind of monoblock type adsorbent of the adsorption oxygen-preparation from air |
| CN111989149A (en) * | 2020-04-14 | 2020-11-24 | 成都盈辰科技有限公司 | Method of movable pressure swing adsorption oxygen production device |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5415683A (en) * | 1993-11-17 | 1995-05-16 | Praxair Technology, Inc. | Vacuum pressure swing adsorption process |
| CN1126585C (en) * | 1999-06-05 | 2003-11-05 | 湖北宜化集团有限责任公司 | Variable-pressure adsorption separating method for simultaneously purifying easy-to-adsorb phase and difficult-to-adsorb phase |
| CN1192813C (en) * | 2001-09-28 | 2005-03-16 | 湖北宜化化工股份有限公司 | Pressure swing adsorption gas separating process to purify easy-to-adsorb phase and hard-to-adsorb phase simultaneously |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101952011A (en) * | 2007-12-12 | 2011-01-19 | Co2Crc技术股份有限公司 | A plant and process for recovering carbon dioxide |
| CN101549240B (en) * | 2009-04-23 | 2011-05-04 | 天津大学 | Method for absorbing methane in condensed coal bed gas through pressure varying mode including carbon dioxide replacement |
| CN109745828A (en) * | 2017-11-03 | 2019-05-14 | 中国科学院大连化学物理研究所 | A kind of monoblock type adsorbent of the adsorption oxygen-preparation from air |
| CN109745828B (en) * | 2017-11-03 | 2021-10-15 | 中国科学院大连化学物理研究所 | Integral adsorbent for oxygen production by adsorption from air |
| CN111989149A (en) * | 2020-04-14 | 2020-11-24 | 成都盈辰科技有限公司 | Method of movable pressure swing adsorption oxygen production device |
| WO2021207906A1 (en) * | 2020-04-14 | 2021-10-21 | 成都盈辰科技有限公司 | Method for mobile pressure swing adsorption oxygen production device |
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