CN102671426B - Isolate and remove the apparatus and method for of air and pollutant - Google Patents
Isolate and remove the apparatus and method for of air and pollutant Download PDFInfo
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- CN102671426B CN102671426B CN201110054407.9A CN201110054407A CN102671426B CN 102671426 B CN102671426 B CN 102671426B CN 201110054407 A CN201110054407 A CN 201110054407A CN 102671426 B CN102671426 B CN 102671426B
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Abstract
The present invention relates to the apparatus and method for for the suspended particulates in liquid such as removing lubricant and fuel etc. and pollutant.Its lubricant recovery system has a water vapor absorption box (140).This water vapor absorption box (140) is made up of super absorbent resin (SAP) (142) being positioned at polyester webs (143) border.SAP extracts and absorbs steam from lubricant or other liquid.SAP containing steam can combine with polyester webs (143), may become gel.One layer polypropylene adsorbent (144) is positioned at the periphery of bounded material (143), guarantees that steam is all deposited in adsorbent layer (144) outside.Optionally resin bed is placed in the liquid stream of discharging from polypropylene adsorbent inner, to absorb suspended particulates from lubricant, can also as barrier harmful ion being exchanged for useful ion.Whole water vapor absorption box can be placed in outer cover or pouch body (162).Pouch body (162) has inflated design, can adjust accordingly along with the volume of SAP increases.Water vapor absorption box can be integrated in the filter containing typical filter element.
Description
Technical field
The present invention is relevant to fluid purification system, especially relevant to the apparatus and method for of the suspended particulates being used for removing in the liquid such as lubricant and fuel and pollutant.
Background technology
The present invention is relevant to liquid purification equipment and method, is particularly useful for the engine using lubricating oil or hydraulic system.Particularly, the invention provides the oil/lubricant processing configuration of several uniqueness, unique system can be formed, make liquid again reach kilter.
Oil reclaimer is that the evaporimeter head that heat-transfer arrangement is housed is merged into inside cavity.Heat-transfer devices can merge deflector, to be formed with the evaporator room of deflector.
Structural element and the making material of oil strainer are varied.Typical filter device comprises the filter medium in filter filling, and is sealed by top arrangement.Mechanical interface (such as hickey) and liquid delivery device (such as oil-in and oil export) are all integrated in top arrangement.Filtering material can be paper products, the filtering material of Prof. Du Yucang and other similar materials.
Oil reclaimer can also comprise the oil additive of solubility in addition, augments oil plant over time, become.Additive in filter, the part between particulate filter material and felt pan.Putting into additive is to contact with oil, and additive can be modulated to and dissolves over time.
Oil reclaimer generally processes these particulates by being discharged in air by suspended particulates.So just have to create the configuration for Control pollution.
Super absorbent resin (SAP) (also referred to as solidifying powder) is a kind of polymer, and it can absorb and retain the huge amount liquid relevant to himself quality.
Water absorbent polymer (being categorized as hydrogel) is by absorbing the aqueous solution with the hydrogen of water molecules.Therefore the water absorbing capacity of SAP depends on the ion concentration of the aqueous solution.In deionized-distilled water, the absorbable moisture of SAP is 500 times (30-60 of himself volume doubly) of himself weight, but when putting it in the salting liquid of 0.9%, water imbibition then significantly declines, 50 times that may only have himself weight.The chemical valence cation of the appearance in solution will hinder polymer and water molecules.
The preparation method that super absorbent resin is commonly used now is mixed with NaOH by acrylic acid, and add initator, makes its polymerization reaction take place generate polyacrylic acid sodium salt (sometimes also referred to as crosslinking sodium polyacrylate).This polymer is the most common sap type prepared by the world today.Also other materials can be used to prepare super absorbent resin, such as: polyacrylamide copolymer, maleic anhydride ethylene copolymer, cross-linked carboxymethyl cellulose, polyvinyl alcohol copolymer, cross linked polyoxyethylene, and the starch graft copolymer of polyacrylonitrile etc.The latter is one of the oldest form of preparation SAP.
Main use two kinds of methods prepare super absorbent resin at present: suspension polymerisation or polymerisation in solution.Two kinds of processes respectively have superiority, and can produce the product of same quality.
Polymerization based on solution is the most frequently used process of current SAP manufacturer.This process not only efficiency is high, and capital cost is usually lower.Solution processes uses water base monomer solution to produce the gel become by polymerization ofathe reactants in a large number.The reaction of polymerization itself can be used (heat release) most of course of reaction to be promoted, contribute to like this reducing production cost.Then make reactive polymeric thing gel cracked, dewater and be pressed into final particle size.Any process carried out to improve SAP performance characteristic all completes usually after the final particle size of formation.
Fewer companies is only had to adopt resuspension procedure, because it needs production control and the product engineering technology of implementing higher degree in the course of the polymerization process.Water-based reactions thing is suspended in hydrocarbon-based solvents by this process.Final result generates principal polymeric particle in the reactor by suspension polymerisation, instead of generate in mechanically stage after the reaction.The stage just completed or can also be reacted in course of reaction and improve performance.
Total water imbibition and expansion volume is determined with the type of crosslinked polymer and degree.The usual water absorbing capacity of SAP that low-density is cross-linked is higher, and degrees of expansion is larger.The SAP of these types also has softer and comparatively sticky gel structure.The polymer that crosslink density is high demonstrates lower water absorbing capacity and degrees of expansion.The intensity of gel is firm, even if bear certain pressure, shape of particle also can remain unchanged.
The general trend of oil recovery process absorbs suspended particulates (such as hydrocarbon), and be discharged in air.This process lacks the consideration to environmental protection aspect, and some country is paying close attention to and to reduce by making laws or to stop this way at present.
Therefore, we are it is desirable that can implement optimally-controlled oil recovery system to purification process.In addition, end user also will be allowed in design to customize purification by multiple stacking array apparatus and monitor configuration.
Summary of the invention
The present invention is applicable to the lubricant recovery system containing recycling box (use is contained in the high absorbency material in polyester webs).Polyester webs is encapsulated in one deck adsorbent.Optionally one deck resin can also be placed between adsorbent and system output port.Reclaimer can be loaded in expandable protective sleeve.
The first, the invention provides the equipment using super absorbent resin (SAP) material (being contained in the polyester webs of composition recycling box) to absorb suspended particulates and water.Recycling box can be loaded in expandable protective sleeve.SAP absorbs steam and combines with it from liquid, and then is combined with polyester webs.
The second, the invention provides one deck adsorbent, the moisture that before can getting rid of, SAP does not absorb completely.
3rd, the present invention uses one deck resin to remove remaining suspended particulates in course of reaction upstream.In addition, tree resin layer also catches the harmful ion entered by ion exchange process, and by useful plasma diffusing W,Mo in lubricant.
4th, the present invention is that recycling box introduces multiple geometric configuration, comprising:
A is similar to volume the overlapping of cake and closes up recycling box;
B forms the winding recycling box of helical core;
C rectangular sachet;
The circular pouch of d;
E star pouch;
The cylindrical pouch of f;
The expandable outer cover of g; And
H has the outer cover of deflector.
Wherein:
The first, recycling box is placed in expansion protective cover.
The second, in single protective cover, place multiple recycling box.
3rd, resin bed is between the outflow district and the discharge orifice of filter of recycling box.
4th, the present invention provides removable recycling box in the recovery filter filtering element containing conventional lubricants.
The invention provides the equipment that can be configured for following purposes:
A is only except anhydrating;
B is except gentle state (suspended particulates) pollutant that anhydrates;
C except anhydrating, gaseous state (suspended particulates) pollutant and sodium ion barrier;
D provides sodium ion barrier.
The present invention can be used for any liquid that may impregnated of steam, comprising:
A automotive fuel,
B oil,
C brake fluid,
D power steering fluid,
E transmission fluid,
F hydraulic fluid,
G and other similar liquids.
The present invention can merge the hydrated calcium sodium potassium aluminosilicate be embedded in polymer (ion-exchange) resin bed, to absorb the gas of hydrocarbon and so on.Or, also can use following silicate:
A sodium potassium aluminosilicate,
B hydrated calcium aluminosilicate,
C hydration sodium aluminum silicate,
D hydrated calcium sodium aluminum silicate,
E hydration sodium potassium calcium aluminium silicate, and
F hydration sodium calcium zeopan.
The personnel being familiar with relevant technological can understand and identify above and other functional parts, Characteristics and advantages of the present invention further with reference to specification hereinafter described, statement and additional pattern.
Accompanying drawing explanation
Fig. 1 is the water vapor absorption equipment partial view corresponding to the present invention's first exemplary components;
Fig. 2 is the isometric view of first the example recycling box being arranged in the other winding-structure key element of resin bed;
Fig. 3 is the top view of recycling box winding assembly;
Fig. 4 is the isometric view of second the example recycling box being arranged in bag structure key element;
Fig. 5 is the pouch recycling box partial view separated from (the 5th part) Fig. 4;
Fig. 6 is the plan view of the 3rd example recycling box collection bag being placed in protective cover;
Fig. 7 is positioned at the other multiple recycling boxes of resin bed, express liquid flow path;
Fig. 8 is the zoomed-in view that impregnated of the high-hydroscopicity particle isometric view of steam to being combined with polyester webs;
Fig. 9 is the equal proportion partial view of the lubricated filter combined with expansion recycling box;
Figure 10 is the partial view at lubricated filter top;
Figure 11 is the facade partial view of lubricated filter, similar with the filter in Fig. 9, has expansion functional part in the sidewall of filter protective cover;
Figure 12 is the isometric view of second lubricated filter module, adds the design of optional inflatable sidewalls;
Figure 13 is the isometric view of the 3rd lubricated filter module, adds outside expansion steam absorption plant;
Figure 14 is the plan fragmentary views of the lubricated filter module separated from (the 14th part) Figure 13;
Figure 15 is the part elevation view of the expansion protective cover holding multiple recycling box;
Figure 16 is the Exemplary of liquid flow graph that steam minimizing technology is described.
Detailed description of the invention
For convenience of description, herein " on ", D score, "left", "right", "front", "rear", " longitudinal direction ", the vocabulary such as " transverse direction " and relevant derivative should with the directional correlation shown in the present invention in FIG.But people will be understood that the present invention also can adopt other different directions and sequence of steps, and for exception, Wen Zhonghui explicitly points out.Therefore, in additional pattern illustrate and the particular device described in following specification and process just embody by exemplary components the invention theory defined in separate statement.So, relevant to assembly described herein specificly to measure with other physical features and nonrestrictive, unless expressly stated otherwise.
Water vapor absorption equipment represents with 100 usually, and it appears in the part elevation view shown in Fig. 1.Water vapor absorption equipment 100 is defined as a reative cell formed, and its filter protective cover sidewall 102 is arranged in tubular structure, and its entrance end wall 104 is positioned at one end of tubular structure, and outlet end wall 106 is positioned at the other end of tubular structure.Filter protective cover sidewall 102 can be random cross-sectional shape, comprises annular, circle, rectangle, polygon etc.Enter opening connector 108 to be positioned on entrance end wall 104, provide input hole 110 to receive inlet flow 112.Water vapor absorption equipment 100 passes through the supply section being connected to liquid recovery system into opening connector 108 removably.Entering opening connector 108 can be any other interface that neck, hickey or the personnel being familiar with this technique know.Discharge connector 114 is positioned on outlet end wall 106, for water vapor absorption equipment 100 provides emission path.Discharge connector 114 provides discharge orifice 116, for carrying out water conservancy diversion to discharge stream 118.Discharge connector 114 preferably with the structural element entering opening connector 108 and conform to.The liquid of fuel, lubricant and so on flows into interior room by inlet flow 112, then inflow filter protective cover sidewall 102 is inner, absorbs steam, then discharged by discharge stream 118 by multiple moisture absorption inserts 120 wherein.Overall flow path is as shown in intermediate flow path 230.
Moisture absorption insert 120 is first exemplary components described in detail in Fig. 2 and Fig. 3.Moisture absorption insert 120 is that the polyester webs 124 by being included super absorbent resin (SAP) 122 reels from core 128 to edge 129.Polypropylene adsorbent 126 is grafted to the outer rim of polyester webs 124, and continues to reel around core.Resin bed 130 can be placed around the discharge end of moisture absorption insert 120, carry out purified treatment further.Super absorbent resin (SAP) 122 is described in the background parts of specification.Liquid enters the arrival end of moisture absorption insert 120, makes liquid comes into contact super absorbent resin (SAP) 122.Super absorbent resin (SAP) 122 can extract and absorb steam from liquid.Absorption process makes the volumetric expansion of super absorbent resin (SAP) 122, and maximum possible expand into 500 times of initial volume.Helical design can allow moisture absorption insert 120 absorb the corresponding expansion of process of steam with super absorbent resin (SAP) 122.Then, be positioned at the other resin bed 130 of moisture absorption insert 120 fluid discharge end and can entrap moisture that is excessive or that escape.Do further process by polypropylene adsorbent 126 pairs of liquid, wherein, polypropylene adsorbent 126 can get rid of excessive water and gel, allows lubricating fluid to flow through.Which adds the chance that super absorbent resin (SAP) 122 absorbs steam.
Fig. 4 is water vapor absorption box 140, and it is selective structure key element, and Fig. 5 is its local side view.Water vapor absorption box 140, containing the material identical with moisture absorption insert 120, is equipped with super absorbent resin (SAP) 142 in polyester webs 143.Polyester webs 143 is arranged in polypropylene adsorbent 144.Expandable sidewall 146 is positioned at the waste side of polypropylene adsorbent 144, as shown in the figure.Water vapor absorption box 140 should be placed on liquid stream inside, make inlet flow 150 enter the entrance side of water vapor absorption box 140, and output stream 152 is discharged from the waste side of water vapor absorption box 140.Super absorbent resin (SAP) 142 can absorb steam, and the volume of super absorbent resin (SAP) 142 particle is increased.The super absorbent resin (SAP) 142 that impregnated of steam can be combined with polyester webs 143, allows the liquid reclaimed flow through polyester webs 143 by output stream 152.This geometrical construction of water vapor absorption box 140 can be expanded.A kind of mode is expanded by expandable sidewall 146, and another kind of mode uses elastomeric material to expand by upper and lower surface, as shown in the figure.Residual steam is got rid of by polypropylene adsorbent 144.Reclaim further by resin bed 148, resin bed 148 can absorb all suspended particulates, such as hydrocarbon.In addition, resin bed 148 also can discharge ion in liquid.The exemplary application of resin bed is just to provide ion-exchange barrier and carries out ion-exchange, such as, be other useful ions by sodium ion exchange.
Resin bed 148 plants diverse ways by three (3) provides two (2) to plant different purposes.The first purposes is removing and catches the suspended particulates polluting tested liquid.The suspended particulates size of removing is needed to be generally 0.1 micron to 0.3 micron.This can be realized by first method, namely, use natural crystal (ore in such as zeolite race) or perlite (convert a kind of volcanic glass rock form with millions of microstructure to, suspended particulates can be comprised after superhigh temperature process).Usually have the minitype channel of 0.1 to 1 micron in the perlite of zeolite and expansion, these passages have sharp-pointed edge, can filter from liquid or block suspended particulates.
The second purposes is releasing beneficial ion in tested liquid.This at least can be realized by three kinds of distinct methods.First method is the extension to above-mentioned removing suspended particulates method.Material for absorbing suspended particulates also can be used for ion exchange process.Catch the sodium ion entered and exchange the useful ion be discharged in tested liquid.By selecting particular ore or using volcano mixture to customize this process.
Second method is by selecting the fluoropolymer resin of Prof. Du Yucang to realize.If do not have this polymer, we just need to use certain adhesive to the perlite of the ore in zeolite race or expansion.The fluoropolymer resin of Prof. Du Yucang can use different useful ions to provide ion-exchange same as described above.
The third method use embedded zeolite, perlite or the two be embedded in compound in resin bed.This compound possesses the advantage of above-mentioned two kinds of methods simultaneously.
Recycling box can be encapsulated in various structural element.The first example package is the absorption pouch 160 entrance end wall 104 being placed in expansion.The absorption pouch 160 expanded comprises bag 162, and wherein have again an inner bag 164, it has at least one to enter opening connector 166 and has an Outlet connector 168 at least.Enter opening connector 166 with the liquid of inner exchanging in provide an entrance port 167, so that tested liquid enters inside.Outlet connector 168 with the liquid of inner exchanging in provide and export port 169, to discharge tested liquid.Inside may be defined as the housing having upper surface, lower surface and be positioned at circumferential surface therebetween.The design at least can provide an entrance port 167 and an outlet port 169, and the former total cross-sectional area is greater than the latter, therefore can form positive internal pressure.The container of dress liquid can be arranged in the objects such as rectangular configuration key element (as shown in the figure), loop configuration key element, pouch containing multiple dilation and folded form pouch.
Multiple water vapor absorption box 140 can be placed in single container and carry out water conservancy diversion, as shown in Figure 7.Inlet flow 150 enters multiple water vapor absorption box 140, then flows to resin bed 148.Resin bed 148 meeting confined liquid stream, pressure in being formed in water vapor absorption box 140.Then liquid will deflection, forms output stream 152, and it is usually vertical with the direction of inlet flow 150.The pressure increased contributes to the absorption process promoting super absorbent resin (SAP) 142, and the process that super absorbent resin (SAP) 142 is combined with polyester webs 143.
A key inventive in removal process uses polyester webs 143 combine and comprise super absorbent resin (SAP) 142.Any method can be used to construct polyester webs 143; Woven net assembly such as shown in figure.Woven net is formed by being woven together by the polyester webs fiber 143b of the polyester webs fiber 143a in many first directions and many second directions.Super absorbent resin (SAP) 142 can absorb steam, generates a material SAP142a containing steam.As shown in the figure, this group can be combined with polyester webs 143 containing the material SAP 142a of steam; But be heated machine oil operating temperature and can add fast response.Super absorbent resin (SAP) 142 can expand because absorbing steam.Water vapor absorption box 140 is arranged in outer cover; This outer cover have employed inflated design, can adapt to the volume increased.Inflated design can be any rational structural element.
Water vapor absorption box 140 can be integrated in the reclaim of lubricant filter of water vapor absorption filtration kit 200 and so on.Can use any rational configuration and the exemplary components of first shown in Fig. 9-11 integrated.Water vapor absorption filtration kit 200, containing common filtration element, is comprised the filtration be fixed on removably in filter base by filter mounting interface 204 and fills with 202 (not shown)s.Generally installed by hickey.One end that water vapor absorption filtration kit 200 faces filter mounting interface 204 is called filter floor 206.Large have one to install sealing ring 208 on the periphery of filtering tank 202, and it extends from the upper surface of filtering tank 202.Sealing ring 208 is installed liquid to be sealed between water vapor absorption filtration kit 200 and filter base.Upper surface has multiple entrance port 210, and liquid is flowed into water vapor absorption filtration kit 200 from system (not shown) by them.The liquid flowed into is shunted by input manifold 212, enters in the expansion absorption container 170 in water vapor absorption filtration kit 200.Water vapor absorption part and filtration fraction, containing filtering tank inner wall device 203, can separate by water vapor absorption filtration kit 200.At least one inwall port 218 (being positioned at the bottom of filtering tank inner wall device 203) provides water vapor absorption filtration kit 200 from water vapor absorption part to the transition of filtration fraction.Multiple water vapor absorption box 140 is positioned at permeable simple filtration material 178, and this filtering material is positioned at again the expansion outer wall 172 of expansion absorption container 170.Liquid flows into expansion absorption container 170 by first expanding end 174, then continues to flow in multiple water vapor absorption box 140.As mentioned before, water vapor absorption box 140 can absorb steam from liquid.Owing to absorbing steam, SAP 122 volume can increase, and expansion outer wall 172 meeting longitudinal dilatation, to adapt to the increase of storage volume, filter floor 206 is reconfigured for expanded configuration 206 ' (shown in dotted line) from original factory configuration (as shown by the solid line).After liquid handling, can be discharged by second of expansion absorption container 170 expanding end 176, flow in expansion area 224.Then liquid continues to flow through inwall port 218, removes process forward suspended particulates removal and filter process to from steam.Resin bed 222 near transition portion, for removing the suspended particulates in liquid.Liquid continues to flow into the filter chamber containing filter membrane 220.Delivery channel 216 can be provided to be emitted by outlet port 214 by liquid.Delivery channel 216 can be hollow, also medium can be housed.
Be the 3rd exemplary components in Figure 12, be called water vapor absorption filtration kit 200b.In the 3rd assembly, filtering tank 202 also can be expanded by filtering tank dilation 240.Expansion adjusting device 242 is equipped with on top, and expansion adjusting device 244 is equipped with in bottom, provides the transition between filtering tank dilation 240 and filtering tank 202.Filtering tank dilation 240 can circumferentially expand, and increases with the volume adapting to super absorbent resin (SAP) 122.Can inflated design be left for designer to decide.
Figure 13 is another kind of configuration, is called that two recycling equipment 250, Figure 14 is its viewgraph of cross-section, describes its water vapor absorption process in detail.Two recycling equipment 250 has two independent recovery section.Two recycling equipment 250 has a shared filtration fraction (wherein having the typical filter assembly described above), also has an independent water vapor absorption part (having oneself independently flow path).The filtering tank 202 that example water vapor absorption part is positioned at filtration fraction is outside.Water vapor absorption part comprises water vapor absorption sidewall 254 (having multiple liquid port 256 by water vapor absorption upper sealing gasket 252) and steam removal unit tap mouth sealing ring 258 (form a circle around water vapor absorption sidewall 254, provide the leak-tight seal between liquid source and reative cell).Inflatable sidewalls part 260 is at least formed along a part of sidewall of water vapor absorption sidewall 254.Inflatable sidewalls part 260 can allow sidewall along with the volume increase generation longitudinal dilatation of super absorbent resin (SAP) 122.Two recycling equipment 250 can comprise various indicator, illustrates and when needs to change water vapor absorption part.Wherein a kind of indicator is the indicator 262 of printing, and when inflatable sidewalls part 260 is shunk, its fuzzy difficulty is distinguished, when inflatable sidewalls part 260 expands, and its clear and legible (replacing indicator 262 ' of printing).This type of indicator of the second is applicable to the independent position on filtering tank 202, and inflatable sidewalls part 260 expands herein, and align with filter replacement index line 264 in water vapor absorption sidewall 254 bottom surface the most at last.The polyester webs 124 of screw winding is formed, containing super absorbent resin (SAP) 122 between the different initial volume winding layer of polyester webs 124 around internal tank 272.Super absorbent resin (SAP) 122 can be wound in internal layer, outwards to expand along spiral helicine each layer.Winding layer can be included in container ectosome 274.Container ectosome 274 can be pleating, to carry out radial expansion.As mentioned before, polypropylene adsorbent 126 can be grafted to the last on one or more layers of winding polyester webs 124.
Water vapor absorption process can be limited in any expansion outer cover.Expansion can be longitudinally (as shown in the exemplary components in Figure 15), along the circumferential direction, radial or wherein any combination.Expand to have come by any known expansion surface 270, such as pleating surface, extensile surface and other similar surfaces.What exemplary components showed is by pleating surface of carrying out longitudinal dilatation.Multiple water vapor absorption box 140 can be placed in the internal tank 272 of expansion surface 270.Expansion surface 270 can be liquid and entraps outer cover and provide access and export (do not show, but easy understand).Or expansion surface 270 also can be the permeable material of sealing, the liquid polluted is allowed to flow through the material included.
The present invention comprises the treatment step of a series of distinct definition, and these steps are as shown in recovery process Figure 30 0 of Figure 16.This process, first according to the step 302 making liquid comes into contact super absorbent resin, makes the heating liquid (such as oil or other lubricants) being subject to steam and/or suspended particulates pollution flow in the water vapor absorption equipment containing super absorbent resin 122.According to water vapor absorption step 304, super absorbent resin 122 can extract and absorb the steam entrapped.SAP can expand because absorbing steam.Then the vapour molecule of SAP and combination is combined with polyester webs again, forms gel.This is called that SAP expands and integrating step 306.According to steam flow quantity control step 308, the steam that SAP does not absorb completely can contact polypropylene adsorbent layer 126.Polypropylene adsorbent layer 126 can get rid of steam, unabsorbed steam before permission SAP absorbs further.Lubricant continues to flow in resin bed through polypropylene adsorbent layer 126, and this is called the eliminating step 310 in adsorbent layer.According to contact pressure resin layer step 312, test lubricant continues to enter resinbed 130.By the suspended particulates entrapped in lubricant or gas before resin bed 130 can absorb, comprises and retain.In addition, useful ion also can be introduced in lubricant by resin bed 130.These operations are called that resin bed activates step 314.The same with removal process described herein, SAP is arranged in the polyester webs 124 forming pouch.Because SAP can continue to absorb steam, SAP can expand at most 500 times of initial volume.SAP is combined with polyester webs 124, forms gel.Pouch expands along with the increase of SAP volume.This is called that SAP pouch is by combining and expansion absorption and the step 316 retaining steam.
Be readily appreciated that, method described herein is implemented by following steps: allow lubricant flow through filter process before step, be then filtration step, or partial lubrication agent flows through the steam parallel with filter process and removes process.This process can be used for gasoline, lubricant (such as oil, power steering fluid, transmission fluid etc.) and other liquid.Can select whether to use resin bed 130.
More than describe and be only applicable to optimal components.Be familiar with personnel and the creation of related process or use personnel of the present invention can modify to the present invention.Therefore be readily appreciated that, in pattern, display is only for reference with the assembly above described, and is not to limit the scope of the invention, and according to Patent Law and principle of legality with equal authenticity, this is explanation explanation by following declaration definition.
Claims (17)
1. a steam separation equipment, this equipment comprises:
A steam separation equipment protective cover, comprises the sidewall that has protective cover and tubular cross-section, and one end of an end wall and sidewall is adjacent, and one end that another end wall is contrary with sidewall is adjacent, and the protective cover that protective cover forms an energy receiving fluids is inner; Described steam separation equipment protective cover comprises a protective cover sidewall, and described steam separation equipment protective cover comprises again at least one expansion functional part further;
At least one passage divides the liquid of protective cover to enter port;
At least one passage divides the fluid discharge port of protective cover;
Flow path of the liquid can enter between port and at least one fluid discharge port at least one liquid and carry out fluid exchange;
The Part I of whole flow path of the liquid crossed over completely by filtering material, and carries out thickness extension along a part for flow path of the liquid;
At least one moisture absorption insert, moisture absorption insert comprises the super absorbent resin being positioned at bounded material, and wherein bounded material is polyester webs at least partially;
At least one moisture absorption insert is positioned at certain position of filtering material inside, moisture absorption insert can be expanded from initial permutation volume, finally cause transposed filtering material;
Filter chamber is positioned at the Part II of flow path of the liquid, and filter chamber comprises filter membrane, can be separated and collect the solid in liquid when liquid flows therethrough;
Flow path is wherein configured to: liquid stream is material after filtration, and wherein a part of liquid flows through at least one moisture absorption insert, and then liquid stream is through filter chamber.
2., according to the steam separation equipment mentioned in claim 1, moisture absorption insert can comprise polypropylene adsorbent further, and it is positioned at polyester webs periphery at least partly.
3., according to the steam separation equipment mentioned in claim 2, moisture absorption insert wherein can expand.
4., according to the steam separation equipment mentioned in claim 3, moisture absorption insert wherein has following a kind of expansion fashion at least:
A) longitudinally,
B) along the circumferential direction, and
C) radial.
5. according to the steam separation equipment mentioned in claim 1, this equipment can comprise resin bed further, in its flow path at moisture absorption insert between outside and at least one fluid discharge port.
6., according to the steam separation equipment mentioned in claim 1, resin bed wherein at least comprises following a kind of material:
A) zeolite,
B) perlite expanded,
C) calcium sodium potassium aluminosilicate,
D) sodium potassium aluminosilicate,
E) hydrated calcium aluminosilicate,
F) hydration sodium aluminum silicate,
G) hydrated calcium sodium aluminum silicate,
H) hydration sodium potassium calcium aluminium silicate, and
I) hydration sodium calcium zeopan.
7., according to the steam separation equipment mentioned in claim 1, moisture absorption insert wherein is at least arranged in following a kind of structural element:
A) reel,
B) be similar to volume the overlapping of cake and close up recycling box,
C) the winding recycling box of helical core is formed,
D) circular pouch;
E) star pouch;
F) cylindrical pouch, and
G) rectangular sachet.
8. a steam separation equipment, this equipment comprises:
A steam separation equipment protective cover, comprises the sidewall that has protective cover and tubular cross-section, and one end of an end wall and sidewall is adjacent, and one end that another end wall is contrary with sidewall is adjacent, and the protective cover that protective cover forms an energy receiving fluids is inner; Described steam separation equipment protective cover comprises a protective cover sidewall, and described steam separation equipment protective cover comprises again at least one expansion functional part further;
At least one passage divides the liquid of protective cover to enter port;
At least one passage divides the fluid discharge port of protective cover;
Flow path of the liquid can enter between port and at least one fluid discharge port at least one liquid and carry out fluid exchange;
A part for whole flow path of the liquid crossed over completely by filtering material, and carries out thickness extension along a part for flow path of the liquid;
At least one moisture absorption insert, moisture absorption insert comprises the super absorbent resin being positioned at bounded material, and wherein bounded material is polyester webs at least partially;
At least one moisture absorption insert is positioned at certain position of filtering material inside, moisture absorption insert can be expanded from initial permutation volume, finally cause transposed filtering material; And
Flow path is wherein configured to: liquid stream is material after filtration, and wherein a part of liquid flows through at least one moisture absorption insert, and then liquid stream is through filter chamber.
9. according to Claim 8 in the steam separation equipment mentioned, moisture absorption insert can comprise polypropylene adsorbent further, and it is positioned at polyester webs periphery at least partly.
10., according to the steam separation equipment mentioned in claim 9, moisture absorption insert wherein can expand.
11. according to the steam separation equipment mentioned in claim 10, wherein be expanded to rare following a kind of mode:
A) longitudinally,
B) along the circumferential direction, and
C) radial.
12. according to Claim 8 in the steam separation equipment mentioned, this equipment can comprise resin bed further, in its flow path at moisture absorption insert between outside and at least one fluid discharge port.
13. according to Claim 8 in the steam separation equipment mentioned, moisture absorption insert wherein is at least arranged in following a kind of structural element:
A) reel,
B) be similar to volume the overlapping of cake and close up recycling box,
3c) form the winding recycling box of helical core,
D) circular pouch;
E) star pouch;
F) cylindrical pouch, and
G) rectangular sachet.
14. according to Claim 8 in the steam separation equipment mentioned, this equipment can comprise expansion absorption container further, wherein comprises an expansion functional part, can extend to parallel with filtering material thickness and length is equal.
15. according to the steam separation equipment mentioned in claim 14, wherein the expanding end of first end wall or second end wall and expansion functional part is adjacent, and therefore, when expansion functional part expands, each adjacent end wall also can be reconfigured for the configuration of extension.
16. according to Claim 8 in the steam separation equipment mentioned, this equipment can comprise expansion absorption container further, wherein comprises an expansion functional part, can extend to parallel with filtering material thickness and length is equal.
17. according to the steam separation equipment mentioned in claim 16, wherein the expanding end of first end wall or second end wall and expansion functional part is adjacent, and therefore, when expansion functional part expands, each adjacent end wall also can be reconfigured for the configuration of extension.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110054407.9A CN102671426B (en) | 2011-03-08 | 2011-03-08 | Isolate and remove the apparatus and method for of air and pollutant |
| HK12113429.0A HK1172579A1 (en) | 2011-03-08 | 2012-12-27 | Air and contaminat isolation and removal apparatus and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110054407.9A CN102671426B (en) | 2011-03-08 | 2011-03-08 | Isolate and remove the apparatus and method for of air and pollutant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102671426A CN102671426A (en) | 2012-09-19 |
| CN102671426B true CN102671426B (en) | 2015-10-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110054407.9A Expired - Fee Related CN102671426B (en) | 2011-03-08 | 2011-03-08 | Isolate and remove the apparatus and method for of air and pollutant |
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| Country | Link |
|---|---|
| CN (1) | CN102671426B (en) |
| HK (1) | HK1172579A1 (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1197690A1 (en) * | 1983-09-30 | 1985-12-15 | Zhurba Mikhail G | Filter for purifying liquids |
| CN1111542A (en) * | 1993-07-01 | 1995-11-15 | 格雷弗公司 | An improved filter and a method for separating charged particles from a liquid stream |
| CN1232403A (en) * | 1996-10-04 | 1999-10-20 | 美国3M公司 | Flow-by solid phase extraction device |
| CN200977424Y (en) * | 2006-09-25 | 2007-11-21 | 林振兴 | Structure improvement of functional purifying and water filtering device |
| CN101385909A (en) * | 2008-09-12 | 2009-03-18 | 天津科技大学 | Extraction method of natural soluble polysaccharide using radial chromatography |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6848584B2 (en) * | 2002-09-26 | 2005-02-01 | Drilltec Patents & Technologies Co., Inc. | Strainer basket and method of making and using the same |
-
2011
- 2011-03-08 CN CN201110054407.9A patent/CN102671426B/en not_active Expired - Fee Related
-
2012
- 2012-12-27 HK HK12113429.0A patent/HK1172579A1/en not_active IP Right Cessation
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1197690A1 (en) * | 1983-09-30 | 1985-12-15 | Zhurba Mikhail G | Filter for purifying liquids |
| CN1111542A (en) * | 1993-07-01 | 1995-11-15 | 格雷弗公司 | An improved filter and a method for separating charged particles from a liquid stream |
| CN1232403A (en) * | 1996-10-04 | 1999-10-20 | 美国3M公司 | Flow-by solid phase extraction device |
| CN200977424Y (en) * | 2006-09-25 | 2007-11-21 | 林振兴 | Structure improvement of functional purifying and water filtering device |
| CN101385909A (en) * | 2008-09-12 | 2009-03-18 | 天津科技大学 | Extraction method of natural soluble polysaccharide using radial chromatography |
Also Published As
| Publication number | Publication date |
|---|---|
| HK1172579A1 (en) | 2013-04-26 |
| CN102671426A (en) | 2012-09-19 |
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