CN102397738A - Vertical bed adsorber - Google Patents
Vertical bed adsorber Download PDFInfo
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- CN102397738A CN102397738A CN2011103497489A CN201110349748A CN102397738A CN 102397738 A CN102397738 A CN 102397738A CN 2011103497489 A CN2011103497489 A CN 2011103497489A CN 201110349748 A CN201110349748 A CN 201110349748A CN 102397738 A CN102397738 A CN 102397738A
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Abstract
The invention discloses a vertical bed adsorber, which comprises an adsorber barrel and an adsorption bed, wherein the adsorber barrel is provided with a gas inlet and a gas outlet; the adsorption bed is arranged in the adsorber barrel; the adsorber barrel is arranged vertically; the adsorption bed is vertically arranged on the middle part of the absorber barrel, and is used for partitioning the absorber barrel into a left gas inlet area and a right gas outlet area; the gas inlet and the gas outlet are formed in the left gas inlet area and the right gas outlet area respectively, and the gas inlet direction of the gas inlet is parallel to the adsorption bed; the left side surface and the right side surface of the adsorption bed are provided with adsorption bed vertical walls formed by laminating metal pore plates and metal meshes. Compared with the prior art, the vertical bed adsorber has the advantages: the service period of an adsorbing agent can be increased, the technical requirements of operation and maintenance on the adsorber are lowered, the running of the adsorber is more stable, safer and more reliable, the installation floor area of equipment is greatly reduced, and the compactness of the entire set of adsorber is improved.
Description
Technical field
The absorber that the present invention relates to use in the Chemical Manufacture, especially a kind of perpendicular bed formula absorber.
Background technology
Absorber is an equipment commonly used in the Chemical Manufacture, is used for purified treatment working medium, in order effectively to remove the impurity in the working medium; Often in an absorber,, use multiple different adsorption agent to different impurity component in the working medium; The component that is prone to most be adsorbed by the impurity composition in the working medium; The optimum absorbent of this component of absorption is arranged on the ground floor of adsorbent bed, removes the impurity that is prone to most be adsorbed in the working medium earlier, and then remove other impurity compositions with another kind of adsorbent.
Shown in Fig. 1 is the absorber in the air separation equipment of prior art; Its structure mainly comprises the horizontally disposed absorber cylindrical shell 1 that is supported by bearing 11; Be horizontally placed on the adsorbent bed 2 in this absorber cylindrical shell 1, the bottom of absorber cylindrical shell 1 is provided with air inlet 3, and the top of absorber cylindrical shell 1 is provided with exhaust outlet 4; Because the absorber cylindrical shell 1 and the adsorbent bed 2 of existing absorber are horizontally disposed; Therefore also be called horizontal absorber, Fig. 2 is the left view of Fig. 1, and Fig. 3 is the A portion structure for amplifying sketch map of Fig. 1.This absorber purpose is used for removing impurity such as airborne moisture, carbon dioxide.Wherein moisture content is adsorbed removing the most easily; Therefore the ground floor of adsorbent bed 2 is the best silica gel absorbers of adsorption moisture; 5 beds; Be used for removing airborne moisture, and then use the impurity such as carbon dioxide in adsorbent of molecular sieve 6 absorbed airs, so adsorbent of molecular sieve 6 has constituted second adsorption bed of absorber.Existing this horizontal adsorber structure, air is silica gel absorber 5 beds of from bottom to top flowing through earlier, gets into adsorbent of molecular sieve 6 beds of the second layer again.In the middle of above-mentioned two kinds of adsorption layers, metal separation net 7 is set, prevent the mixing of silica gel absorber 5 and adsorbent of molecular sieve 6.
Behind the air entering absorber, what at first impact is the metal perforated plate 8 of adsorbent bed 2 lower planes and the horizontal mattress of woven wire 9 compositions, and this horizontal mattress has been born the weight of whole adsorbents and the important function that even distribution air flow stream is crossed adsorbent bed 2.When in a single day air velocity took place by serious the variation, the effect that horizontal mattress is uniformly distributed with air-flow reduced greatly, causes the local area at adsorbent bed 2; Air velocity can reach and drive the degree that adsorbent flows, and the horizontality on the last plane 10 of adsorbent of molecular sieve 6 free laies is destroyed: the place that air velocity is high, and adsorbent of molecular sieve 6 is blown away; Fall the low place of air velocity, thereby cause the absorption of adsorbent of molecular sieve 6 highly seriously not wait, recover just often in operating mode; Reduce because of the air current flow resistance increases air flow rate in the place of adsorbent of molecular sieve 6 bed thickness (height), opposite; 6 layers of thin place of adsorbent of molecular sieve; Increase because of the air current flow resistance reduces air flow rate, in these regional areas, adsorbent of molecular sieve 6 adsorb saturated soon (because of the few air flow stream flow of quantity of sorbent many again); So compelled having to of the adsorption cycle of adsorbent bed 2 reduces, and had a strong impact on the normal operation of equipment.Can reduce the life cycle of adsorbent when serious significantly.And when stop changing adsorbent when having to, be again a very thing of trouble: when adsorbent takes out, the workman in absorber, little by little to claw, take a lot of work, require great effort, work situation, condition are very poor, and when reinstalling, condition is also similar.Therefore, the user really goes to war, and has shortened the very long ordinary production cycle when changing adsorbent.
Hence one can see that: in the process of this air-flow adsorbent bed 2 of flowing through from bottom to top, the lower plane of ground floor adsorbent bed is extremely important: 1. it will bear the weight of all adsorbents; 2. be to guarantee that all adsorbent beds become horizontal basis; 3. be bear air inlet 3 gas shocks try hard to keep the card critical point, equally distributed first road of air-flow.Therefore, especially in large-scale absorber, the structural design of this air-flow windward side seems extremely important.And the last plane of first adsorption bed (the i.e. metal separation net 7 of two kinds of adsorbents; Also be the lower plane of second adsorption bed) structural design; Then seem than being easier to; Only play and isolate the effect that adsorbent and air-flow distribute again and get final product, do not work to bear the second adsorbent bed weight, the weight of second adsorption bed is directly delivered on first adsorption bed.And the last plane of second adsorption bed is free and open.Hence one can see that, and first adsorption bed receives the restriction on two planes up and down, and this first adsorption bed is fixed basically, and its thickness of bed layer is also fixed basically.And in second adsorption bed; Because the last plane of adsorbent is free unconfined, therefore is in operation and runs into, the air-flow of the absorber serious non-uniform phenomenon of meeting generation that distributes because operating accident produces the pressure flow velocity of absorber when changing suddenly; Directly can be washed into plane on the adsorbent of level rugged; Cause the inhomogeneous of adsorption bed thickness, thereby aggravated the non-uniform phenomenon that air-flow distributes, can produce the air-flow short circuit when serious and cause the absorber adsorption cycle to lose efficacy; The compelled maintenance of stopping (utilize on the adsorbent plane to take off the flat-bed machine structure, take off adsorbent flat again).When this maintenance process often takes place, can obviously shorten the service life of adsorbent, have to the package unit parking change adsorbent.In this horizontal absorber, changing adsorbent is again the trouble of a time-consuming effort, and several days ability of often will stopping work is accomplished.Directly influenced the economic benefit (having increased personnel's the work time cost etc. of cost, shut-down direct economic loss expense, the maintenance of adsorbent) of applying unit.
Secondly, large-size horizontal absorber floor space is big, and the compactedness of package unit is poor, and the country that this is had a large population in a small area concerning us, problem is particularly outstanding and urgent.
Summary of the invention
The objective of the invention is to: a kind of perpendicular bed formula absorber is provided; Can improve the life cycle of adsorbent; Reduction is to the specification requirement of absorber Operation and Maintenance; The operation that makes absorber more steadily, more safe and reliable, reduce the installation floor space of equipment greatly, improve the compactedness of absorber package unit.
For realizing above-mentioned purpose, the present invention can take following technical proposals:
A kind of perpendicular bed formula absorber of the present invention comprises the absorber cylindrical shell that is provided with gas feed and gas discharge outlet, is arranged at the adsorbent bed in the said absorber cylindrical shell, and said absorber cylindrical shell is to erect to be provided with; Said adsorbent bed vertically be arranged at the middle part of absorber cylindrical shell and with the absorber cylindrical shell at a distance from telling left part air inlet area and right part exhaust area; Said gas feed is parallel with adsorbent bed with the airintake direction that gas discharge outlet is arranged at left part air inlet area and right part exhaust area and gas feed respectively, is equipped with the adsorbent bed straight wall wall that is stacked together and constituted by metal perforated plate and woven wire on the left and right side surface of adsorbent bed.
The discharge directions of said gas discharge outlet is parallel with adsorbent bed.
When in said adsorbent bed, being provided with a kind of adsorbent, the upper cover body of the absorber cylindrical shell of adsorbent top end is provided with the adsorbent charging door, and the low head body of the absorber cylindrical shell of adsorbent bottom end position is provided with the adsorbent discharge port; When in said adsorbent bed, being provided with two or more adsorbent; Isolating silk screen by the metal of vertical setting between horizontal layering setting of each adsorbent and the adjacent two layers adsorbent separates; Be equipped with corresponding adsorbent charging door on the upper cover body of the absorber cylindrical shell of every kind of adsorbent top end, be equipped with corresponding adsorbent discharge port on the low head body of the absorber cylindrical shell of every kind of adsorbent bottom end position.
Said gas feed and gas discharge outlet all are arranged on the said upper cover body, or all are arranged on the said low head body.
The percent opening of said metal perforated plate is more than or equal to 50%, and the aperture of said woven wire is smaller or equal to 70% of the absorbent particles average diameter, and said metal is isolated the average diameter of the aperture of silk screen smaller or equal to less adsorbent; The stacked of metal perforated plate and woven wire fixed with rivet; The said adsorbent bed straight wall wall outside vertically is provided with stiffener, and this stiffener utilizes bolt to be fixedly connected with metal perforated plate, woven wire and the two ends up and down of this stiffener are fixedly connected with the low head body with the upper cover body respectively.
Said metal perforated plate is to be spliced to form by polylith metal perforated plate unit, and said woven wire is spliced to form by polylith woven wire unit, and metal perforated plate is positioned at the outside of woven wire.
The lower end of said absorber cylindrical shell is provided with bearing.
The bottom of said low head body is provided with skirt support.
Compare with the horizontal absorber of prior art; The invention has the beneficial effects as follows: owing to adopt technique scheme, said absorber cylindrical shell is to erect to be provided with, said adsorbent bed vertically be arranged at the middle part of absorber cylindrical shell and with the absorber cylindrical shell at a distance from telling left part air inlet area and right part exhaust area; Said gas feed is parallel with adsorbent bed with the airintake direction that gas discharge outlet is arranged at left part air inlet area and right part exhaust area and gas feed respectively; Be equipped with the adsorbent bed straight wall wall that is stacked together and constituted by metal perforated plate and woven wire on the left and right side surface of adsorbent bed, the absorber of this structure changes vertical this measure through the absorber cylindrical shell by horizontal; The floor space that equipment is installed just reduces greatly; The compactedness of package unit further improves, and the country that especially this is had a large population in a small area concerning us, it is particularly important that this point seems; Because the airintake direction of gas feed is parallel with adsorbent bed; When air-flow got into absorber, air-flow did not directly impact the metal perforated plate and the woven wire of adsorbent bed, and air-flow 90 degree of will turning just get into adsorbent bed; So the percussion that perpendicular formula absorber adsorbent bed of the present invention receives air inlet gas is very little; Be arranged on the adsorbent bed straight wall wall on adsorbent bed left and right side surface, the weight of no longer bearing all adsorbents, only play hold, fixed absorbent and be uniformly distributed with the effect of air-flow; Certainly also to bear air communication and cross adsorbent bed front and back action of pressure; And the windward side is born the effect of gas shock power and is compared with horizontal absorber and want much little, maybe can ignore, therefore; The present invention is more much lower than the requirement of strength of the horizontal mattress in the corresponding windward side of horizontal adsorbent bed to the requirement of adsorbent bed straight wall wall intensity, and this just can reduce the production cost of adsorbent bed straight wall wall; Clearly; The metal perforated plate of adsorbent bed left and right side and woven wire have immobilized the absorption height (distance of airflow passes) of adsorbent; Thoroughly eliminated absorber when operation, because of the adsorbent bed bed height absorber that causes that changes moves abnormal accident.
Further beneficial effect is: when in said adsorbent bed, being provided with a kind of adsorbent, the upper cover body of the absorber cylindrical shell of adsorbent top end is provided with the adsorbent charging door, and the low head body of the absorber cylindrical shell of adsorbent bottom end position is provided with the adsorbent discharge port; When in said adsorbent bed, being provided with two or more adsorbent; Isolating silk screen by the metal of vertical setting between horizontal layering setting of each adsorbent and the adjacent two layers adsorbent separates; Be equipped with corresponding adsorbent charging door on the upper cover body of the absorber cylindrical shell of every kind of adsorbent top end, be equipped with corresponding adsorbent discharge port, this structure on the low head body of the absorber cylindrical shell of every kind of adsorbent bottom end position; Owing to be provided with adsorbent charging door and adsorbent discharge port; Therefore absorber can not add adsorbent when dispatching from the factory, and the direct shipping user of adsorbent is in the on-the-spot interpolation of user installation; The beneficial effect that this improvement brings is: 1. the freight charges of adsorbent can reduce greatly, and transportation route, handling and loading number of times can significantly reduce; 2. because the volume of large-scale absorber is original just very big; Weight is also very heavy; If when tens tons adsorbent refilled in the absorber, weight can increase the weight of more, make overweight often of the transportation of large-scale absorber; If remove adsorbent and can become not overweight transportation part, freight can be saved a lot; 3. when adsorbent dispatched from the factory in factory, the seal of inner wrapping often, adsorbent were difficult for being polluted easily; But when putting into absorber, packing of it is destroyed, in charging and transportation; Be easy to by atmosphere pollution, have to before driving, carry out high-temperature activation and handle, cause be affected the service life of adsorbent; If adsorbent is in user's preceding interpolation of driving, that situation has very big change, because adsorbent is activation when dispatching from the factory; The charging back drives to use at once, and minimum activation temperature, time can reduce, to being of great benefit to the service life of adsorbent.Because adsorbent charging door, discharge port are separately positioned on the upper and lower end in the corresponding adsorbent zone, therefore, when the charging of adsorbent and discharging; Because adsorbent can flow freely; The workman can operate outside absorber, needn't get in the container just can accomplish the adsorbent loading and unloading, the process of changing or loading and unloading adsorbent; Become a job that is easy to operate, thoroughly changed the idea in horizontal absorber epoch.When in the adsorbent bed multiple adsorbent being arranged; Metal to be set between two kinds of adsorbents isolate silk screen; The intensity of this metal isolation silk screen is more much lower than the intensity of adsorbent bed both sides straight wall wall; Only play and isolate adsorbent and get final product with the effect that is uniformly distributed with air-flow, but the operating process during to adsorbent loading and unloading material has proposed strict requirement: during independent a kind of adsorbent charge and discharge operations, this metal of handlebar is isolated the danger of silk screen breaking-up! And every kind of adsorbent is provided with corresponding adsorbent charging door and adsorbent discharge port, can load and unload synchronously by multiple adsorbent, can effectively avoid this danger.
Further beneficial effect is again: because said gas feed and gas discharge outlet all are arranged on the said upper cover body; Or all be arranged on the said low head body; This structure; The import and export of gas are arranged on the same termination of absorber, and the flow that can make air communication cross the adsorption bed everywhere in theory equates, thereby the even distribution of gas is more guaranteed.And the structure of the horizontal absorber of this point can't guarantee theoretically.
Description of drawings
Fig. 1 is the structural representation of the horizontal absorber in the air separation equipment of prior art;
Fig. 2 is the left view of Fig. 1;
Fig. 3 is the A portion structure for amplifying sketch map of Fig. 1;
Fig. 4 is the structural representation of the specific embodiment of the invention;
Fig. 5 be Fig. 4 the upper cover body overlook the structure for amplifying sketch map;
Fig. 6 be Fig. 4 the low head body look up the structure for amplifying sketch map;
Fig. 7 is the local structure for amplifying sketch map of the adsorbent bed of Fig. 4;
Fig. 8 is the A portion structure for amplifying sketch map of Fig. 7;
Fig. 9 is that the B-B of Fig. 7 is to the structure for amplifying sketch map.
The specific embodiment
Shown in Fig. 4 to 9; A kind of perpendicular bed formula absorber of the present invention; Comprise an absorber cylindrical shell 3; This absorber cylindrical shell 3 comprises a upper cover body 301 and a low head body 302, and absorber cylindrical shell 3 is erect and is provided with, adsorbent bed 4 vertically be arranged at the middle part of absorber cylindrical shell 3 and with absorber cylindrical shell 3 at a distance from telling left part air inlet area 5 and right part exhaust areas 6; Gas feed 1 is arranged at respectively on the low head body 302 of left part air inlet area 5 and right part exhaust area 6 with gas discharge outlet 2; And the airintake direction of gas feed 1 is parallel with adsorbent bed 4, and the discharge directions of gas discharge outlet 2 is parallel with adsorbent bed 4, is equipped with the adsorbent bed straight wall wall 9 that is stacked together and constituted by metal perforated plate 7 and woven wire 8 on the left and right side surface of adsorbent bed 4; Metal perforated plate 7 is positioned at the outside of woven wire 8; The percent opening of metal perforated plate 7 is minimum to be 50%, is preferably 70%, and the aperture of the woven wire 8 of silica gel absorber 17 1 sides equals 70% of silica gel absorber 17 average diameter of particles; The aperture of the woven wire 8 of adsorbent of molecular sieve 18 1 sides equals 70% of adsorbent of molecular sieve 18 average diameter of particles, and the aperture that said metal is isolated silk screen 10 equals the average diameter that less adsorbent is adsorbent of molecular sieve 18 particles; In order to strengthen stacked fastness, rivet with rivet 16 between metal perforated plate 7 and the woven wire 8.Said adsorbent bed straight wall wall 9 outsides vertically are provided with stiffener 13; This stiffener 13 utilizes bolt 14 to be fixedly connected with metal perforated plate 7, woven wire 8, and the two ends up and down of this stiffener 13 are connected with low head body 302 usefulness bolt with upper cover body 301 respectively.
Because metal perforated plate 7 areas are very big; And will be from the manhole of absorber (the absorber manhole is the conventional design of this area in the shift-in absorber cylindrical shell 3; Figure of description its position of not drawing), thus metal perforated plate 7 must be made up of polylith metal perforated plate unit could shift-in, secondly the rigidity of metal perforated plate 7 and woven wire 8 itself need to strengthen; In view of above factor; So flanging (be placed on middle part, flanging is all wanted on four limits) together after metal perforated plate 7 and the riveted joint of woven wire 8 subdivisions, the height principle of flanging is the binding that makes things convenient for bolt 19 when being higher than unit and unit combination.The principle of subdivision is: vertical dimension is long as far as possible, make unit number few as far as possible, and the size of width and unit number is to depend on from the manhole of absorber, to move on to metal perforated plate Unit 7, woven wire unit 8 in the absorber cylindrical shell 3.In said adsorbent bed 4, be provided with silica gel absorber 17 and adsorbent of molecular sieve 18 from left to right successively; Isolating silk screen 10 by the metal of vertical setting between this two layers of adsorbents separates; The upper cover body 301 of silica gel absorber 17 top ends is provided with silica gel absorber 17 charging doors 11; The upper cover body 301 of adsorbent of molecular sieve 18 top ends is provided with adsorbent of molecular sieve 18 charging doors 11 '; The low head body 302 of silica gel absorber 17 bottom end positions is provided with silica gel absorber 17 discharge ports 12, and the low head body 302 of adsorbent of molecular sieve 18 bottom end positions is provided with adsorbent of molecular sieve 18 discharge ports 12 '.The bottom of low head body 302 is provided with skirt support 15, and the power of expanding with heat and contract with cold of absorber is compensated by gas feed 1 and gas discharge outlet 2 tube connectors, and this point collocation structure that expands with heat and contract with cold than horizontal absorber again is simple, easy and effective.
The superior degree of performance, structure of the perpendicular bed of the present invention formula absorber substantially exceeds existing absorber.But owing to increased layer of metal orifice plate 7 and woven wire 8 than horizontal absorber; Be to have increased the flow through flow resistance of adsorbent bed of gas in theory; But the argumentation through above-mentioned several respects superiority can be known; The overall flow resistances of gas descends, moreover can also be when designing and calculating, the unfavorable factor of coming the commensurate structure design to bring through various means (like suitable reduction flow velocity etc.).
Claims (8)
1. one kind is erected bed formula absorber; Comprise the absorber cylindrical shell (3) that is provided with gas feed (1) and gas discharge outlet (2); Be arranged at the adsorbent bed (4) in the said absorber cylindrical shell (3), it is characterized in that: said absorber cylindrical shell (3) is to erect to be provided with; Said adsorbent bed (4) vertically be arranged at the middle part of absorber cylindrical shell (3) and with absorber cylindrical shell (3) at a distance from telling left part air inlet area (5) and right part exhaust area (6); It is parallel with adsorbent bed (4) with the airintake direction of right part exhaust area (6) and gas feed (1) that said gas feed (1) and gas discharge outlet (2) are arranged at left part air inlet area (5) respectively, is equipped with the adsorbent bed straight wall wall (9) that is stacked together and constituted by metal perforated plate (7) and woven wire (8) on the left and right side surface of adsorbent bed (4).
2. perpendicular bed formula absorber according to claim 1, it is characterized in that: the discharge directions of said gas discharge outlet (2) is parallel with adsorbent bed (4).
3. perpendicular bed formula absorber according to claim 2 is characterized in that:
When in said adsorbent bed (4), being provided with a kind of adsorbent; The upper cover body (301) of the absorber cylindrical shell (3) of adsorbent top end is provided with adsorbent charging door (11), and the low head body (302) of the absorber cylindrical shell (3) of adsorbent bottom end position is provided with adsorbent discharge port (12);
When in said adsorbent bed (4), being provided with two or more adsorbent; Isolating silk screen (10) by the metal of vertical setting between horizontal layering setting of each adsorbent and the adjacent two layers adsorbent separates; Be equipped with corresponding adsorbent charging door (11) on the upper cover body (301) of the absorber cylindrical shell (3) of every kind of adsorbent top end, be equipped with corresponding adsorbent discharge port (12) on the low head body (302) of the absorber cylindrical shell (3) of every kind of adsorbent bottom end position.
4. perpendicular bed formula absorber according to claim 3, it is characterized in that: said gas feed (1) and gas discharge outlet (2) all are arranged on the said upper cover body (301), or all are arranged on the said low head body (302).
5. perpendicular bed formula absorber according to claim 4; It is characterized in that: the percent opening of said metal perforated plate (7) is more than or equal to 50%; The aperture of said woven wire (8) is smaller or equal to 70% of absorbent particles average diameter, and said metal is isolated the average diameter of the aperture of silk screen (10) smaller or equal to less adsorbent; The stacked of metal perforated plate (7) and woven wire (8) fixed with rivet (16); Said adsorbent bed straight wall wall (9) outside vertically is provided with stiffener (13), and this stiffener (13) utilizes bolt (14) to be fixedly connected with metal perforated plate (7), woven wire (8) and the two ends up and down of this stiffener (13) are fixedly connected with low head body (302) with upper cover body (301) respectively.
6. perpendicular bed formula absorber according to claim 5; It is characterized in that: said metal perforated plate (7) is to be spliced to form by polylith metal perforated plate unit; Said woven wire (8) is spliced to form by polylith woven wire unit, and metal perforated plate (7) is positioned at the outside of woven wire (8).
7. perpendicular bed formula absorber according to claim 1 and 2, it is characterized in that: the lower end of said absorber cylindrical shell (3) is provided with bearing (15).
8. perpendicular bed formula absorber according to claim 6, it is characterized in that: the bottom of said low head body (302) is provided with skirt support.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2011103497489A CN102397738A (en) | 2011-11-08 | 2011-11-08 | Vertical bed adsorber |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2011103497489A CN102397738A (en) | 2011-11-08 | 2011-11-08 | Vertical bed adsorber |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103212272A (en) * | 2013-04-17 | 2013-07-24 | 中空能源设备有限公司 | Vertical modular molecular sieve adsorber |
| CN106582199A (en) * | 2016-12-30 | 2017-04-26 | 华北水利水电大学 | Vertical molecular sieve adsorber with lateral gas entering |
| CN106844974A (en) * | 2017-01-24 | 2017-06-13 | 武汉旭日华环保科技股份有限公司 | The method and device of absorber optimization |
| CN107441881A (en) * | 2017-09-22 | 2017-12-08 | 杭州杭氧股份有限公司 | A kind of annular space bag web frame of vertical type radial flow adsorber |
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| CN2334481Y (en) * | 1997-06-09 | 1999-08-25 | 黄自元 | Organic waste gas purifing equipment |
| CN2875564Y (en) * | 2005-12-06 | 2007-03-07 | 刘朝轩 | Vertical gas filter |
| CN101987276A (en) * | 2010-08-12 | 2011-03-23 | 苏州顶裕节能设备有限公司 | Horizontal activated carbon absorption tower |
| CN202289810U (en) * | 2011-11-08 | 2012-07-04 | 杭州中泰深冷技术股份有限公司 | Vertical-bed adsorber |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN2165919Y (en) * | 1993-10-27 | 1994-05-25 | 杜渭元 | Combined vertical adsorption layer waste gas purifier |
| CN2334481Y (en) * | 1997-06-09 | 1999-08-25 | 黄自元 | Organic waste gas purifing equipment |
| CN2875564Y (en) * | 2005-12-06 | 2007-03-07 | 刘朝轩 | Vertical gas filter |
| CN101987276A (en) * | 2010-08-12 | 2011-03-23 | 苏州顶裕节能设备有限公司 | Horizontal activated carbon absorption tower |
| CN202289810U (en) * | 2011-11-08 | 2012-07-04 | 杭州中泰深冷技术股份有限公司 | Vertical-bed adsorber |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103212272A (en) * | 2013-04-17 | 2013-07-24 | 中空能源设备有限公司 | Vertical modular molecular sieve adsorber |
| CN106582199A (en) * | 2016-12-30 | 2017-04-26 | 华北水利水电大学 | Vertical molecular sieve adsorber with lateral gas entering |
| CN106844974A (en) * | 2017-01-24 | 2017-06-13 | 武汉旭日华环保科技股份有限公司 | The method and device of absorber optimization |
| CN107441881A (en) * | 2017-09-22 | 2017-12-08 | 杭州杭氧股份有限公司 | A kind of annular space bag web frame of vertical type radial flow adsorber |
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Application publication date: 20120404 |