CN203653242U - Five-tower pressure swing adsorption nitrogen making device - Google Patents
Five-tower pressure swing adsorption nitrogen making device Download PDFInfo
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- CN203653242U CN203653242U CN201420026985.0U CN201420026985U CN203653242U CN 203653242 U CN203653242 U CN 203653242U CN 201420026985 U CN201420026985 U CN 201420026985U CN 203653242 U CN203653242 U CN 203653242U
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Abstract
The utility model discloses a five-tower pressure swing adsorption nitrogen making device comprising an absorption tower A, an absorption tower B, an absorption tower C, an absorption tower D, an absorption tower E, an emptying manifold, an air inlet manifold, a nitrogen discharging manifold, a boosting manifold, a first-stage pressure equalizing manifold, a second-stage pressure equalizing manifold and a concurrent air escape butter tank. The lower ends of the absorption tower A, the absorption tower B, the absorption tower C, the absorption tower D and the absorption tower E are respectively and fixedly provided with a branch emptying pipe A, a branch emptying pipe B, a branch emptying pipe C, a branch emptying pipe D and a branch emptying pipe E, and the upper ends of the absorption tower A, the absorption tower B, the absorption tower C, the absorption tower D and the absorption tower E are respectively and fixedly provided with a branch nitrogen discharging pipe A, a branch nitrogen discharging pipe B, a branch nitrogen discharging pipe C, a branch nitrogen discharging pipe D and a branch nitrogen discharging pipe E. The five-tower pressure swing adsorption nitrogen making device can be used for effectively increasing the yield and purity of nitrogen while increasing the recovery rate of nitrogen gas in the adsorption towers.
Description
Technical field
the utility model relates to nitrogen-making device technical field, is a kind of five tower swing adsorption nitrogen producing apparatus.
Background technology
tradition making nitrogen by pressure swing adsorption process using pressure swing adsorption process, it is PSA method, taking air as raw material, carbonaceous molecular sieve is sorbent material, pressurize by adsorption bed, combined cyclical operation process reduces pressure, utilization is full of the molecular sieve of microporous crystal to gas molecule selective adsorption, make molecular diameter enter carbonaceous molecular sieve duct than the little oxygen of nitrogen with VELOCITY DIFFUSION faster, the absorption of being preferred property, in short period of time, oxygen is enriched in rapidly carbon molecular sieve particles inside (solid phase), nitrogen does not have enough time to be adsorbed and is enriched in gas phase, thereby reaching oxygen nitrogen separates, and obtain a kind of air-making nitrogen technology of nitrogen.It adopts two adsorption towers, in air, the separation of oxygen, nitrogen is to carry out in turn between two adsorption towers, by time variable control trip valve, make an adsorption tower in pressurization adsorbed state, another adsorption tower is in normal pressure desorption state, and nitrogen is produced in two tower alternations, by two tower parallel connections, the pressurization that hockets is adsorbed and decompress(ion) regeneration, thereby obtains continuous nitrogen gas stream.But current existing pressure-variable adsorption legal system nitrogen exists following subject matter: 1, due to carbonaceous molecular sieve constantly sedimentation in adsorption tower, must add carbonaceous molecular sieve, now two tower making nitrogen by pressure swing adsorption must a whole set of Nitrogen plant group be shut down processing, have a strong impact on downstream work; 2, arbitrary nitrogen adsorption tower equipment appurtenance processed, program-controlled valve break down, and a whole set of Nitrogen plant group must be shut down processing, and without backup means, single complete equipment can not ensure continuous long-term operation, and turndown ratio is little; 3, in the time that two towers are all pressed, do not produce nitrogen, produce discontinuous, the nitrogen flow of nitrogen, pressure transient, have a strong impact on downstream nitrogen user's steady running; 4, carbonaceous molecular sieve desorb, regeneration not thorough, nitrogen gas purity is lower, carbonaceous molecular sieve is short work-ing life; 5, the rate of recovery of nitrogen in adsorption tower is low, causes waste; 6, produce nitrogen gas purity be less than 99.99%, nitrogen gas purity is low.
Summary of the invention
the utility model provides a kind of five tower swing adsorption nitrogen producing apparatus; overcome the deficiency of above-mentioned prior art; it can effectively solve existing two tower making nitrogen by pressure swing adsorption (PSA) and have equipment failure, must a whole set of Nitrogen plant group while adding molecular sieve shuts down and process; can not ensure the continuous long-term operation of nitrogen processed; turndown ratio is little, has a strong impact on downstream work, and nitrogen gas purity is lower; carbonaceous molecular sieve is short work-ing life, and the nitrogen in adsorption tower can not reclaim and the low problem of nitrogen gas purity.
the technical solution of the utility model realizes by following measures: a kind of five tower swing adsorption nitrogen producing apparatus, comprise A adsorption tower, B adsorption tower, C adsorption tower, D adsorption tower, E adsorption tower, emptying house steward, inlet manifold, denitrogen house steward, the house steward of boosting, one-level all press house steward, secondary all press house steward and along venting surge tank, at A adsorption tower, B adsorption tower, C adsorption tower, the lower end of D adsorption tower and E adsorption tower is installed with respectively A emptying arm, B emptying arm, C emptying arm, D emptying arm and E emptying arm, A emptying arm, B emptying arm, C emptying arm, the other end of D emptying arm and E emptying arm is fixedly installed togather with emptying house steward respectively, at A emptying arm, B emptying arm, C emptying arm, on D emptying arm and E emptying arm, be installed with respectively A air intake branch, B air intake branch, C air intake branch, D air intake branch and E air intake branch, A air intake branch, B air intake branch, C air intake branch, the other end of D air intake branch and E air intake branch is fixedly installed togather with inlet manifold respectively, at A adsorption tower, B adsorption tower, C adsorption tower, the upper end of D adsorption tower and E adsorption tower is installed with respectively A denitrogen arm, B denitrogen arm, C denitrogen arm, D denitrogen arm and E denitrogen arm, A denitrogen arm, B denitrogen arm, C denitrogen arm, the other end of D denitrogen arm and E denitrogen arm is fixedly installed togather with denitrogen house steward respectively, is installed with respectively the A arm that boosts on A denitrogen arm, A one-level equaler and A secondary equaler are installed with respectively the B arm that boosts on B denitrogen arm, B one-level equaler and B secondary equaler are installed with respectively the C arm that boosts on C denitrogen arm, C one-level equaler and C secondary equaler are installed with respectively the D arm that boosts on D denitrogen arm, D one-level equaler and D secondary equaler are installed with respectively the E arm that boosts on E denitrogen arm, E one-level equaler and E secondary equaler, the A arm that boosts, the B arm that boosts, the C arm that boosts, D arm and the E arm that boosts that boosts is put into the other end and is fixedly installed togather with the blind dead house steward of boosting in two ends respectively, A one-level equaler, B one-level equaler, C one-level equaler, the other end of D one-level equaler and E one-level equaler all presses house steward to be fixedly installed togather with the blind dead one-level in two ends respectively, A secondary equaler, B secondary equaler, C secondary equaler, the other end of D secondary equaler and E secondary equaler all presses house steward to be fixedly installed togather with the blind dead secondary in two ends respectively, denitrogen house steward and boost and be installed with pipe connecting between house steward, secondary is all pressed house steward and along being installed with between venting surge tank along venting pipe connecting, is all pressed between house steward and suitable venting surge tank and be installed with washpipe in one-level, at the A denitrogen arm near denitrogen house steward, B denitrogen arm, C denitrogen arm, on D denitrogen arm and E denitrogen arm, be installed with respectively control valve, at the A emptying arm near emptying house steward, B emptying arm, C emptying arm, on D emptying arm and E emptying arm, be installed with respectively control valve, at A air intake branch, B air intake branch, C air intake branch, D air intake branch, E air intake branch, A one-level equaler, B one-level equaler, C one-level equaler, D one-level equaler, E one-level equaler, the A arm that boosts, the B arm that boosts, the C arm that boosts, the D arm that boosts, the E arm that boosts, A secondary equaler, B secondary equaler, C secondary equaler, D secondary equaler, E secondary equaler, on pipe connecting and suitable venting pipe connecting, be installed with respectively control valve, on washpipe, be installed with respectively pressure regulator valve.
the utility model reasonable and compact in structure; easy to use, in raising adsorption tower, in rate of recovery of nitrogen, can effectively improve and produce nitrogen amount and nitrogen gas purity; and the nitrogen in can efficient recovery adsorption tower; effectively extend the work-ing life of carbonaceous molecular sieve, and turndown ratio is large, in equipment failure, while adding molecular sieve; can not shut down processing; can be continuously macrocyclicly produce nitrogen processed, strong guarantee downstream nitrogen user's steady running, turndown ratio is large.
Brief description of the drawings
accompanying drawing 1 is the process structure schematic diagram of the utility model most preferred embodiment.
coding in accompanying drawing is respectively: 1 is A adsorption tower, 2 is B adsorption tower, 3 is C adsorption tower, 4 is D adsorption tower, 5 is E adsorption tower, 6 is A emptying arm, 7 is B emptying arm, 8 is C emptying arm, 9 is D emptying arm, 10 is E emptying arm, 11 is emptying house steward, 12 is A air intake branch, 13 is B air intake branch, 14 is C air intake branch, 15 is D air intake branch, 16 is E air intake branch, 17 is inlet manifold, 18 is A denitrogen arm, 19 is B denitrogen arm, 20 is C denitrogen arm, 21 is D denitrogen arm, 22 is E denitrogen arm, 23 is denitrogen house steward, 24 is the A arm that boosts, 25 is A one-level equaler, 26 is A secondary equaler, 27 is the B arm that boosts, 28 is B one-level equaler, 29 is B secondary equaler, 30 is the C arm that boosts, 31 is C one-level equaler, 32 is C secondary equaler, 33 is the D arm that boosts, 34 is D one-level equaler, 35 is D secondary equaler, 36 is the E arm that boosts, 37 is E one-level equaler, 38 is E secondary equaler, 39 is the house steward of boosting, 40 all press house steward for one-level, 41 all press house steward for secondary, 42 is pipe connecting, 43 is along venting surge tank, 44 is along venting pipe connecting, 45 is washpipe, 46 is control valve, 47 is pressure regulator valve.
Embodiment
the utility model is not subject to the restriction of following embodiment, can determine concrete embodiment according to the technical solution of the utility model and practical situation.
in the utility model, for convenience of description, the description of the relative position relation of each parts is to be all described according to the Butut mode of Figure of description 1, as: the position relationship of upper and lower, left and right etc. is to determine according to the Butut direction of Figure of description.
below in conjunction with embodiment and accompanying drawing, the utility model is further described:
as shown in Figure 1, this five towers swing adsorption nitrogen producing apparatus comprise A adsorption tower 1, B adsorption tower 2, C adsorption tower 3, D adsorption tower 4, E adsorption tower 5, emptying house steward 11, inlet manifold 17, denitrogen house steward 23, boost house steward 39, one-level all press house steward 40, secondary all press house steward 41 and along venting surge tank 43, at A adsorption tower 1, B adsorption tower 2, C adsorption tower 3, the lower end of D adsorption tower 4 and E adsorption tower 5 is installed with respectively A emptying arm 6, B emptying arm 7, C emptying arm 8, D emptying arm 9 and E emptying arm 10, A emptying arm 6, B emptying arm 7, C emptying arm 8, the other end of D emptying arm 9 and E emptying arm 10 is fixedly installed togather with emptying house steward 11 respectively, at A emptying arm 6, B emptying arm 7, C emptying arm 8, on D emptying arm 9 and E emptying arm 10, be installed with respectively A air intake branch 12, B air intake branch 13, C air intake branch 14, D air intake branch 15 and E air intake branch 16, A air intake branch 12, B air intake branch 13, C air intake branch 14, the other end of D air intake branch 15 and E air intake branch 16 is fixedly installed togather with inlet manifold 17 respectively, at A adsorption tower 1, B adsorption tower 2, C adsorption tower 3, the upper end of D adsorption tower 4 and E adsorption tower 5 is installed with respectively A denitrogen arm 18, B denitrogen arm 19, C denitrogen arm 20, D denitrogen arm 21 and E denitrogen arm 22, A denitrogen arm 18, B denitrogen arm 19, C denitrogen arm 20, the other end of D denitrogen arm 21 and E denitrogen arm 22 is fixedly installed togather with denitrogen house steward 23 respectively, is installed with respectively the A arm 24 that boosts on A denitrogen arm 18, A one-level equaler 25 and A secondary equaler 26 are installed with respectively the B arm 27 that boosts on B denitrogen arm 19, B one-level equaler 28 and B secondary equaler 29 are installed with respectively the C arm 30 that boosts on C denitrogen arm 20, C one-level equaler 31 and C secondary equaler 32 are installed with respectively the D arm 33 that boosts on D denitrogen arm 21, D one-level equaler 34 and D secondary equaler 35 are installed with respectively the E arm 36 that boosts on E denitrogen arm 22, E one-level equaler 37 and E secondary equaler 38, the A arm 24 that boosts, the B arm 27 that boosts, the C arm 30 that boosts, D the boost the other end of arm 36 of arm 33 and E that boosts is fixedly installed togather with the blind dead house steward 39 of boosting in two ends respectively, A one-level equaler 25, B one-level equaler 28, C one-level equaler 31, the other end of D one-level equaler 34 and E one-level equaler 37 all presses house steward 40 to be fixedly installed togather with the blind dead one-level in two ends respectively, A secondary equaler 26, B secondary equaler 29, C secondary equaler 32, the other end of D secondary equaler 35 and E secondary equaler 38 all presses house steward 41 to be fixedly installed togather with the blind dead secondary in two ends respectively, denitrogen house steward 23 and boost and be installed with pipe connecting 42 between house steward 39, secondary is all pressed house steward 41 and along being installed with between venting surge tank 43 along venting pipe connecting 44, is all pressed between house steward 40 and suitable venting surge tank 43 and be installed with washpipe 45 in one-level, at the A denitrogen arm 18 near denitrogen house steward 23, B denitrogen arm 19, C denitrogen arm 20, on D denitrogen arm 21 and E denitrogen arm 22, be installed with respectively control valve 46, at the A emptying arm 6 near emptying house steward 11, B emptying arm 7, C emptying arm 8, on D emptying arm 9 and E emptying arm 10, be installed with respectively control valve 46, at A air intake branch 12, B air intake branch 13, C air intake branch 14, D air intake branch 15, E air intake branch 16, A one-level equaler 25, B one-level equaler 28, C one-level equaler 31, D one-level equaler 34, E one-level equaler 37, the A arm 24 that boosts, the B arm 27 that boosts, the C arm 30 that boosts, the D arm 33 that boosts, the E arm 36 that boosts, A secondary equaler 26, B secondary equaler 29, C secondary equaler 32, D secondary equaler 35, E secondary equaler 38, on pipe connecting 42 and suitable venting pipe connecting 44, be installed with respectively control valve 46, on washpipe 45, be installed with respectively pressure regulator valve 47.A adsorption tower 1, B adsorption tower 2, C adsorption tower 3, D adsorption tower 4 and E adsorption tower 5 are respectively the nitrogen adsorption tower processed in PSA Nitrogen plant technical field in existing known technology, A adsorption tower 1, B adsorption tower 2, C adsorption tower 3, the height of D adsorption tower 4 and E adsorption tower 5 is identical with the height of the nitrogen adsorption tower processed in existing PSA Nitrogen plant technical field, but A adsorption tower 1, B adsorption tower 2, C adsorption tower 3, single tower volume of D adsorption tower 4 and E adsorption tower 5 only has 40% of nitrogen adsorption tower list tower volume processed in existing PSA Nitrogen plant technical field, because aspect ratio is larger, unstripped gas is more easily uniformly distributed, be difficult for producing bias current, it is more abundant that carbonaceous molecular sieve utilizes, in gas, impurity is difficult for penetrating, made nitrogen gas purity more coca according to the adsorption tower of the utility model device, can make the high-purity nitrogen of nitrogen gas purity more than 99.99%, be the conventional surge tank in existing known technology along venting surge tank 43.
now describe whole nitrogen producing craft step program process as an example of A adsorption tower 1 example, the technological process of B adsorption tower 2, C adsorption tower 3, D adsorption tower 4 and E adsorption tower 5 is identical with A adsorption tower 1.Sequential control sketch of the present utility model is as shown in table 1, the A representative absorption in table 1, and ED1 represents an equal step-down, ED2 represents two equal step-downs, P representative is along putting regeneration, and D represents inverse put regeneration, and regeneration is rinsed in PP representative, ER1 represents that one all boosts, and ER2 represents that one all boosts, and 0 representative is waited for.
table 1
| Step order | 1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 9 | 10 | 11 | 12 | 13 | 14 | 15 |
| A adsorption tower | A | A | A | ED1 | ED2 | P | D | PP | PP | PP | ER2 | 0 | ER1 | FR | FR |
| B adsorption tower | ER1 | FR | FR | A | A | A | ED1 | ED2 | P | D | PP | PP | PP | ER2 | 0 |
| C adsorption tower | PP | ER2 | 0 | ER1 | FR | FR | A | A | A | ED1 | ED2 | P | D | PP | PP |
| D adsorption tower | D | PP | PP | PP | ER2 | 0 | ER1 | FR | FR | A | A | A | ED1 | ED2 | P |
| E adsorption tower | ED1 | ED2 | P | D | PP | PP | PP | ER2 | 0 | ER1 | FR | FR | A | A | A |
step order 1 to 3, absorption (A): the control valve 46 of unstripped gas (air) on A air intake branch enters A adsorption tower 1 and adsorb, wherein the impurity component except nitrogen is adsorbed by the interior carbonaceous molecular sieve of A adsorption tower 1, A adsorption tower 1 adsorb saturated after, stop absorption, obtain purity and be greater than the control valve 46 of 99.99% high purity product nitrogen on A denitrogen arm 18 and discharged by the tower top of A adsorption tower 1.
step order 4, one equal step-down (ED1): after adsorption process completes, open the control valve 46 on A one-level equaler 25 and C one-level equaler 31, by pipeline, the nitrogen of A adsorption tower 1 interior elevated pressures is put into and just completed the two C adsorption towers 3 that all boost, until the pressure of A adsorption tower 1 and 3 liang of towers of C adsorption tower equates substantially, this process is not only C adsorption tower 3 process of boosting, and reclaim the nitrogen in A adsorption tower 1 bed dead space, the absorb leading-edge of A adsorption tower 1 will continue to pass forward in this course, but not reach yet outlet.
the equal step-down of step order 5: two (ED2) is one after all the process of falling completes, open the control valve 46 on A secondary equaler 26 and D secondary equaler 35, by pipeline, the nitrogen of A adsorption tower 1 interior elevated pressures is put into and just completed the D adsorption tower 4 that rinses regeneration, all boost for two of D adsorption tower 4, this process continues to reclaim the nitrogen in A adsorption tower 1 bed dead space, the absorb leading-edge of A adsorption tower 1 also will continue to pass forward simultaneously, but not reach yet outlet.
step order 6, along putting regeneration (P): after two equal step-down processes complete, open control valve 46 and suitable venting pipe connecting 44 on A secondary equaler 26, the nitrogen of A adsorption tower 1 interior elevated pressures is put into along venting surge tank 43, until the Pressure Drop of A adsorption tower 1 is to required pressure, the nitrogen that this process is further recycled in A adsorption tower 1 bed dead space is used as flushing regeneration source of the gas, and the absorb leading-edge of A adsorption tower 1 also will continue to pass forward simultaneously, and substantially reach outlet.
step order 7, inverse put regeneration (D): along letting slip after journey completes, the absorb leading-edge of A adsorption tower 1 reaches bed outlet substantially, at this moment open the control valve 46 on A emptying arm 6, against absorption direction by A adsorption tower 1 Pressure Drop to close to normal pressure, the impurity being now adsorbed starts to desorb from sorbent material.
step order 8 to 10, rinse regeneration (PP): after inverse put finishes, open the control valve 46 on A emptying arm 6 and A one-level equaler, by A adsorption tower 1 being rinsed after pressure regulator valve 47 adjust fluxes, at this moment the impurity being adsorbed desorbs in a large number along with the reduction of its dividing potential drop, flushing process finishes, and adsorbent reactivation completes, and A adsorption tower 1 is by the two equal boost phases that proceed to thereafter.
step order 14 to 15, the gas product process (FR) of boosting:
after secondary boost pressure process, A adsorption tower 1 pressure does not still reach adsorptive pressure, at this moment open control valve 46 and pipe connecting 42 that A boosts on arm 24, by product nitrogen gas, A adsorption tower 1 is slowly boosted, until A adsorption tower 1 pressure rises to adsorptive pressure.
through above-mentioned a series of step-down and boost after process, A adsorption tower 1 has just completed whole regenerative process, for absorption is next time got ready and enters thus next sorption cycle.
in the time adding molecular sieve, arbitrary nitrogen adsorption tower equipment appurtenance processed, by-pass valve control and break down, can switch to fault adsorption tower or pipeline is closed by time variable control control valve, not needing a whole set of Nitrogen plant group to shut down processes, can realize the on-line maintenance to fault tower by automatically cutting tower program (can switch to double column pressure swing absorption, three tower pressure-variable adsorptions, four tower making nitrogen by pressure swing adsorption), can be continuously macrocyclicly produce nitrogen processed, ensure downstream nitrogen user's steady running, turndown ratio is large; Solve and when traditional making nitrogen by pressure swing adsorption technique is all pressed, do not produced nitrogen, the problem of nitrogen flow, pressure transient.
adopt the utility model nitrogen processed, in the case of adopting the nitrogen-preparing carbon molecular sieves of same quality and quantity, compare existing making nitrogen by pressure swing adsorption product nitrogen amount and can improve 12% to 15%, the rate of recovery has improved 17%, nitrogen production cost processed has reduced by 17%, and can produce continuously nitrogen, nitrogen gas purity has improved 5/1000ths, by smart nitrogen to normal pressure desorb after desorption tower rinse (being pressure equalizing), the impurity being adsorbed on carbonaceous molecular sieve can be cemented out, the adsorptive power of smart pyridine on carbonaceous molecular sieve is very little simultaneously, very easily desorb, carbonaceous molecular sieve desorb like this, regenerate comparatively thorough, be conducive to improve nitrogen gas purity, extend carbonaceous molecular sieve work-ing life, adding carbonaceous molecular sieve or arbitrary nitrogen adsorption tower equipment appurtenance processed, when by-pass valve control breaks down, can be switched to two tower making nitrogen by pressure swing adsorption by time variable control, not needing a whole set of Nitrogen plant group to shut down processes, can be continuously macrocyclicly produce nitrogen processed, ensure downstream nitrogen user's steady running, turndown ratio is large, solve and when traditional making nitrogen by pressure swing adsorption technique is all pressed, do not produced nitrogen, the problem of nitrogen flow, pressure transient.
above technical characterictic has formed most preferred embodiment of the present utility model, and it has stronger adaptability and best implementation result, can increase and decrease according to actual needs non-essential technical characterictic, meets the demand of different situations.
Claims (1)
1. five tower swing adsorption nitrogen producing apparatus, it is characterized in that comprising A adsorption tower, B adsorption tower, C adsorption tower, D adsorption tower, E adsorption tower, emptying house steward, inlet manifold, denitrogen house steward, the house steward of boosting, one-level all press house steward, secondary all press house steward and along venting surge tank, at A adsorption tower, B adsorption tower, C adsorption tower, the lower end of D adsorption tower and E adsorption tower is installed with respectively A emptying arm, B emptying arm, C emptying arm, D emptying arm and E emptying arm, A emptying arm, B emptying arm, C emptying arm, the other end of D emptying arm and E emptying arm is fixedly installed togather with emptying house steward respectively, at A emptying arm, B emptying arm, C emptying arm, on D emptying arm and E emptying arm, be installed with respectively A air intake branch, B air intake branch, C air intake branch, D air intake branch and E air intake branch, A air intake branch, B air intake branch, C air intake branch, the other end of D air intake branch and E air intake branch is fixedly installed togather with inlet manifold respectively, at A adsorption tower, B adsorption tower, C adsorption tower, the upper end of D adsorption tower and E adsorption tower is installed with respectively A denitrogen arm, B denitrogen arm, C denitrogen arm, D denitrogen arm and E denitrogen arm, A denitrogen arm, B denitrogen arm, C denitrogen arm, the other end of D denitrogen arm and E denitrogen arm is fixedly installed togather with denitrogen house steward respectively, is installed with respectively the A arm that boosts on A denitrogen arm, A one-level equaler and A secondary equaler are installed with respectively the B arm that boosts on B denitrogen arm, B one-level equaler and B secondary equaler are installed with respectively the C arm that boosts on C denitrogen arm, C one-level equaler and C secondary equaler are installed with respectively the D arm that boosts on D denitrogen arm, D one-level equaler and D secondary equaler are installed with respectively the E arm that boosts on E denitrogen arm, E one-level equaler and E secondary equaler, the A arm that boosts, the B arm that boosts, the C arm that boosts, D arm and the E arm that boosts that boosts is put into the other end and is fixedly installed togather with the blind dead house steward of boosting in two ends respectively, A one-level equaler, B one-level equaler, C one-level equaler, the other end of D one-level equaler and E one-level equaler all presses house steward to be fixedly installed togather with the blind dead one-level in two ends respectively, A secondary equaler, B secondary equaler, C secondary equaler, the other end of D secondary equaler and E secondary equaler all presses house steward to be fixedly installed togather with the blind dead secondary in two ends respectively, denitrogen house steward and boost and be installed with pipe connecting between house steward, secondary is all pressed house steward and along being installed with between venting surge tank along venting pipe connecting, is all pressed between house steward and suitable venting surge tank and be installed with washpipe in one-level, at the A denitrogen arm near denitrogen house steward, B denitrogen arm, C denitrogen arm, on D denitrogen arm and E denitrogen arm, be installed with respectively control valve, at the A emptying arm near emptying house steward, B emptying arm, C emptying arm, on D emptying arm and E emptying arm, be installed with respectively control valve, at A air intake branch, B air intake branch, C air intake branch, D air intake branch, E air intake branch, A one-level equaler, B one-level equaler, C one-level equaler, D one-level equaler, E one-level equaler, the A arm that boosts, the B arm that boosts, the C arm that boosts, the D arm that boosts, the E arm that boosts, A secondary equaler, B secondary equaler, C secondary equaler, D secondary equaler, E secondary equaler, on pipe connecting and suitable venting pipe connecting, be installed with respectively control valve, on washpipe, be installed with respectively pressure regulator valve.
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| CN201420026985.0U CN203653242U (en) | 2014-01-16 | 2014-01-16 | Five-tower pressure swing adsorption nitrogen making device |
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| CN201420026985.0U CN203653242U (en) | 2014-01-16 | 2014-01-16 | Five-tower pressure swing adsorption nitrogen making device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103787285A (en) * | 2014-01-16 | 2014-05-14 | 新疆独山子天利高新技术股份有限公司 | Five-tower pressure swing adsorption (PSA) nitrogen generating device |
| CN107399719A (en) * | 2016-05-18 | 2017-11-28 | 乔治洛德方法研究和开发液化空气有限公司 | The VSA type oxygen generation methods of periodic regeneration |
| CN108717286A (en) * | 2018-05-25 | 2018-10-30 | 杭州天利空分设备制造有限公司 | A kind of dual controller control method |
| CN112892154A (en) * | 2021-01-22 | 2021-06-04 | 山东津挚环保科技有限公司 | Sled dress pressure swing adsorption equipment |
-
2014
- 2014-01-16 CN CN201420026985.0U patent/CN203653242U/en not_active Withdrawn - After Issue
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103787285A (en) * | 2014-01-16 | 2014-05-14 | 新疆独山子天利高新技术股份有限公司 | Five-tower pressure swing adsorption (PSA) nitrogen generating device |
| CN103787285B (en) * | 2014-01-16 | 2015-10-28 | 新疆独山子天利高新技术股份有限公司 | Five tower swing adsorption nitrogen producing apparatus |
| CN107399719A (en) * | 2016-05-18 | 2017-11-28 | 乔治洛德方法研究和开发液化空气有限公司 | The VSA type oxygen generation methods of periodic regeneration |
| CN108717286A (en) * | 2018-05-25 | 2018-10-30 | 杭州天利空分设备制造有限公司 | A kind of dual controller control method |
| CN108717286B (en) * | 2018-05-25 | 2020-07-21 | 杭州天利空分设备制造有限公司 | Double-controller control method |
| CN112892154A (en) * | 2021-01-22 | 2021-06-04 | 山东津挚环保科技有限公司 | Sled dress pressure swing adsorption equipment |
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