CN214780913U - Novel high-speed full room resin interchanger - Google Patents
Novel high-speed full room resin interchanger Download PDFInfo
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- CN214780913U CN214780913U CN202120704892.9U CN202120704892U CN214780913U CN 214780913 U CN214780913 U CN 214780913U CN 202120704892 U CN202120704892 U CN 202120704892U CN 214780913 U CN214780913 U CN 214780913U
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Abstract
The utility model discloses a novel high-speed full-chamber resin exchanger, which belongs to the field of exchangers and comprises an exchanger body, wherein the upper end inside the exchanger body is fixedly connected with an upper porous plate, the middle position of the exchanger body is fixedly connected with a middle porous plate, the lower end of the exchanger body is fixedly connected with a lower porous plate, the upper porous plate is fixedly connected with a plurality of upper water caps, the middle porous plate is fixedly connected with a plurality of middle water caps, and the upper end of the exchanger body is fixedly connected with an upper inlet and a lower outlet, the device integrates an upper exchange chamber and a lower exchange chamber which are connected in series, can improve the water production, reduce the acid (or alkali) consumption, simultaneously reduce the device volume and the occupied area, and increase the protection of the exchanger body through the connection of an upper reinforcing ring, a lower reinforcing ring and a reinforcing rib, and through the connection of a supporting leg and a supporting plate, an ejector pad, an anti-skid sleeve and an anti-skid block, the steadiness of the support when being placed is increased, and the phenomenon that the exchanger body inclines and falls is avoided.
Description
Technical Field
The utility model relates to an interchanger field, more specifically say, relate to a novel full room resin interchanger of high speed.
Background
The water contains many inorganic salts, such as calcium and magnesium salts. The salt can not be found in water at normal temperature by naked eyes, but brings many troubles to life, such as boiler structure, product quality reduction and the like. The content of calcium and magnesium ions in water is usually expressed by the index "hardness". Hardness 1 degree corresponds to 10 mg of calcium oxide per liter of water. Water with a temperature lower than 8 ℃ is called soft water, water with a temperature higher than 17 ℃ is called hard water, and water with a temperature between 8 and 17 ℃ is called medium hard water. Rain, snow water, river and lake water are soft water, and spring water, deep well water and sea water are hard water. The high-speed full-chamber resin exchanger is a sodium ion exchanger; through this kind of high-speed full room resin exchanger, accomplish the purpose that high hard water once softened, novel high-speed full room resin exchanger is higher thinner moreover, places the steadiness not good, and it is askew to collide the slope easily to take place.
SUMMERY OF THE UTILITY MODEL
To the problem that exists among the prior art, an object of the utility model is to provide a novel full room resin interchanger of high speed, two series connection exchange rooms about this equipment integration, both can improve the system water yield, can reduce sour (or alkali) consumption again, the equipment volume has still been reduced simultaneously, area is reduced, and through last reinforcing ring, lower reinforcing ring is connected with the reinforcement muscle, the protection to the interchanger body has been increaseed, be connected through supporting leg and backup pad, the kicking block, the fore-set, the setting of antiskid cover and non slipping spur, the steadiness when having increaseed the support and placing, avoid the interchanger body to take place the askew phenomenon of slope.
In order to solve the above problems, the utility model adopts the following technical proposal.
A novel high-speed full-chamber resin exchanger comprises an exchanger body, wherein an upper porous plate is fixedly connected to the upper end inside the exchanger body, a middle porous plate is fixedly connected to the middle position of the exchanger body, a lower porous plate is fixedly connected to the lower end of the exchanger body, a plurality of water feeding caps are fixedly connected to the upper porous plate, a plurality of middle water caps are fixedly connected to the middle porous plate, an upper inlet and an upper outlet are fixedly connected to the upper end of the exchanger body, a lower inlet and a lower outlet are fixedly connected to the lower end of the exchanger body, an upper pipeline is fixedly connected to the upper end of the upper inlet and the upper reinforcing ring is fixedly connected to the upper end outside of the exchanger body, a lower reinforcing ring is fixedly connected to the lower end outside of the exchanger body, a plurality of supporting legs are fixedly connected to the lower end of the exchanger body, and supporting plates are fixedly connected to the lower ends of the supporting legs, the utility model discloses a support for the heat exchanger, including the bottom of backup pad, the bottom of backup pad is connected with the bottom of fore-set respectively and is connected with the antiskid cover, this equipment integration two upper and lower series exchange rooms, both can improve the system water yield, can reduce sour (or alkali) again and consume, still reduced equipment volume simultaneously, reduced area, and through last reinforcing ring, lower reinforcing ring is connected with the reinforcement muscle, strengthened the protection to the exchanger body, through being connected of supporting leg and backup pad, the setting of top, fore-set, antiskid cover and antiskid block has increaseed the steadiness when supporting and placing, avoid the exchanger body to take place the askew phenomenon of slope.
Furthermore, a plurality of lower water caps are fixedly connected to the lower porous plate, a plurality of porous plate supports are fixedly connected to the exchanger body, and 2 layers 1751 of semi-hard rubber are lined on the inner wall of the high-speed full-chamber resin exchanger to enhance the corrosion resistance of the equipment and prolong the service life of the equipment.
Further, the lower extreme fixedly connected with lower pipeline of importing and exporting down, the one end of going up the pipeline and the one end of lower pipeline fixedly connected with joint respectively, high-speed full room resin interchanger divide into upper and lower two rooms by upper, middle and lower three perforated plates, and upper and lower perforated plate is equipped with single lamination formula water cap, and middle perforated plate is equipped with double lamination formula water cap.
Furthermore, a plurality of reinforcing ribs are fixedly connected to the exchanger body, the upper reinforcing ring is fixedly connected with the lower reinforcing ring through the reinforcing ribs, perforated plate pillars are additionally arranged between the upper perforated plate, the middle perforated plate and the lower perforated plate to enhance the stability of the perforated plate and the equipment, the lower weak resin is arranged, the upper strong resin is arranged, the upper part of each chamber is filled with a layer of inert resin, and the upper part of each chamber has a floating bed state during operation and adopts countercurrent regeneration.
Further, a plurality of non slipping spur of lower extreme fixedly connected with of antiskid cover, the material of antiskid cover is made for rubber, and the non slipping spur has increaseed placing the steadiness of antiskid cover to make kicking block and fore-set place more firm, avoid the askew phenomenon of inclining of interchanger body emergence.
Compared with the prior art, the utility model has the advantages of:
(1) this two series connection exchange chambers about this equipment is integrated, both can improve the system water yield, can reduce sour (or alkali) consumption again, still reduced equipment volume simultaneously, reduced area, and through last reinforcing ring, lower reinforcing ring and reinforcing rib's being connected, strengthened the protection to the interchanger body, through being connected of supporting leg and backup pad, kicking block, fore-set, antiskid cover and non slipping spur's setting, strengthened the steadiness when placing of support, avoid the interchanger body to take place the askew phenomenon of slope.
(2) The lower porous plate is fixedly connected with a plurality of lower water caps, the exchanger body is fixedly connected with a plurality of porous plate supports, and the inner wall of the high-speed full-chamber resin exchanger is lined with 2 layers 1751 of semi-hard rubber for enhancing the corrosion resistance of equipment and prolonging the service life of the equipment.
(3) The lower end of the lower inlet and outlet is fixedly connected with a lower pipeline, one end of the upper pipeline and one end of the lower pipeline are respectively and fixedly connected with a joint, the high-speed full-chamber resin exchanger is divided into an upper chamber and a lower chamber by an upper porous plate, a middle porous plate and a lower porous plate, the upper porous plate and the lower porous plate are provided with single-lamination type water caps, and the middle porous plate is provided with a double-lamination type water cap.
(4) The exchanger body is fixedly connected with a plurality of reinforcing ribs, the upper reinforcing ring is fixedly connected with the lower reinforcing ring through the reinforcing ribs, perforated plate pillars are added between the upper perforated plate, the middle perforated plate and the lower perforated plate to enhance the mechanical stability of the perforated plates and equipment, the lower weak resin is filled at the lower part, the upper strong resin is filled at the upper part, and the upper part of the resin of each chamber is filled with a layer of inert resin, so that the exchanger has a floating bed state during operation and adopts countercurrent regeneration.
(5) A plurality of non slipping spur of lower extreme fixedly connected with of antiskid cover, the material of antiskid cover is made for rubber, and the non slipping spur has increaseed placing the steadiness of antiskid cover to make kicking block and fore-set place more firm, avoid the askew phenomenon of slope of interchanger body emergence.
Drawings
FIG. 1 is a partial sectional view of the overall structure of the present invention;
FIG. 2 is a schematic view of the overall structure of the present invention;
fig. 3 is a bottom view of the support plate of the present invention;
fig. 4 is a bottom cross-sectional view of the joint of the upper reinforcing ring and the reinforcing rib of the present invention.
The reference numbers in the figures illustrate:
the device comprises an exchanger body 1, an upper porous plate 2, a middle porous plate 3, a lower porous plate 4, an upper water cap 5, a middle water cap 6, a lower water cap 7, a porous plate support column 8, an upper inlet and an outlet 9, a lower inlet and an outlet 10, an upper pipeline 11, a lower pipeline 12, a joint 13, an upper reinforcing ring 14, a lower reinforcing ring 15, reinforcing ribs 16, supporting legs 17, a supporting plate 18, an ejector block 19, an ejector column 20, an anti-slip sleeve 21 and an anti-slip block 22.
Detailed Description
The technical solution in the embodiment of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiment of the present invention; obviously, the described embodiments are only a part of the embodiments of the present invention, and not all embodiments, and all other embodiments obtained by those skilled in the art without any inventive work are within the scope of the present invention based on the embodiments of the present invention.
Referring to fig. 1-4, a novel high-speed full-chamber resin exchanger comprises an exchanger body 1, referring to fig. 1-2, an upper porous plate 2 is fixedly connected to the inner upper end of the exchanger body 1, a middle porous plate 3 is fixedly connected to the middle position of the exchanger body 1, a lower porous plate 4 is fixedly connected to the lower end of the exchanger body 1, a plurality of upper water caps 5 are fixedly connected to the upper porous plate 2, a plurality of middle water caps 6 are fixedly connected to the middle porous plate 3, an upper inlet 9 is fixedly connected to the upper end of the exchanger body 1, a lower inlet 10 is fixedly connected to the lower end of the exchanger body 1, an upper pipeline 11 is fixedly connected to the upper end of the upper inlet 9, an upper reinforcing ring 14 is fixedly connected to the outer upper end of the exchanger body 1, a lower reinforcing ring 15 is fixedly connected to the outer lower end of the exchanger body 1, and a plurality of support legs 17 are fixedly connected to the lower end of the exchanger body 1, the lower extreme fixedly connected with backup pad 18 of supporting leg 17, a plurality of kicking blocks 19 of lower extreme fixedly connected with of backup pad 18, the lower extreme intermediate position fixedly connected with fore-set 20 of backup pad 18, the lower extreme difference joint of kicking block 19 and fore-set 20 has antiskid cover 21, two series connection exchange rooms about this equipment is integrated, both can improve the water yield, but also can reduce sour (or alkali) and consume, still reduced the equipment volume simultaneously, area has been reduced, and through last reinforcing ring 4, lower reinforcing ring 5 is connected with reinforcing rib 6, the protection to interchanger body 1 has been increaseed, through the connection of supporting leg 17 and backup pad 18, kicking block 19, the fore-set 20, antiskid cover 21 and antiskid 22's setting, the steadiness when having increaseed to support and placing, avoid interchanger body 1 to take place the phenomenon that the slope is askew.
Referring to fig. 1, a plurality of lower water caps 7 are fixedly connected to a lower porous plate 4, a plurality of porous plate support columns 8 are fixedly connected to an exchanger body 1, 2 layers 1751 of semi-hard rubber are lined on the inner wall of a high-speed full-chamber resin exchanger to enhance the corrosion resistance of the equipment and prolong the service life of the equipment, a lower pipeline 12 is fixedly connected to the lower end of a lower inlet/outlet 10, a joint 13 is fixedly connected to one end of an upper pipeline 11 and one end of the lower pipeline 12 respectively, the high-speed full-chamber resin exchanger is divided into an upper chamber and a lower chamber by an upper porous plate, a middle porous plate and a lower porous plate, single-lamination water caps are installed on the upper porous plate and the lower porous plate, and a double-lamination water cap is installed on the middle porous plate.
Referring to fig. 2, the exchanger body 1 is fixedly connected with a plurality of reinforcing ribs 16, the upper reinforcing ring 14 is fixedly connected with the lower reinforcing ring 15 through the reinforcing ribs 16, perforated plate pillars are added between the upper perforated plate and the middle perforated plate, the perforated plate pillars are used for enhancing the mechanism stability of the perforated plate and the equipment, the lower resin is weak, the upper resin is strong, the upper resin of each chamber is filled with a layer of inert resin, the upper resin has a floating bed state during operation, countercurrent regeneration is adopted, the lower end of the anti-slip sleeve 21 is fixedly connected with a plurality of anti-slip blocks 22, the anti-slip sleeve 21 is made of rubber, and the anti-slip blocks 22 increase the placing stability of the anti-slip sleeve 21, so that the top blocks 19 and the top pillars 20 are placed more stably, and the phenomenon that the exchanger body 1 inclines and falls is avoided.
When in operation, water enters from the bottom of the exchanger, passes through the porous plate and the water cap, under the action of water flow, the weak resin and the inert resin in the lower chamber are supported, a floating layer with the thickness of about 100mm is formed on the upper part of the water distribution device, the upper part of the floating layer is provided with the compaction resin layer, after the water and the weak resin are subjected to ion exchange, the water passes through the double-lamination type water cap of the middle porous plate, a certain flow velocity is formed in the upper chamber, the floating resin layer is also formed, the compaction strong resin layer is formed on the floating resin layer, the water is subjected to ion exchange again, the treated water flows out from the top of the exchanger, the regeneration liquid of the high-speed full-chamber resin exchanger enters from the top of the exchanger, passes through the water distribution cap at a certain regeneration flow velocity and concentration, passes through the inertia resin layer to uniformly distribute the regeneration liquid, the compaction resin layer is regenerated, and then the water distribution cap is distributed through the middle porous plate, the weak type resin to lower room is regenerated in the same way, make it resume exchange capacity, this equipment integration two upper and lower series connection exchange rooms, both can improve the water yield, can reduce acid (or alkali) consumption again, still reduced equipment volume simultaneously, area has been reduced, and through last reinforcing ring 4, lower reinforcing ring 5 and reinforcing rib 6's being connected, strengthened the protection to interchanger body 1, through the connection of supporting leg 17 and backup pad 18, kicking block 19, kicking post 20, antiskid cover 21 and non slipping spur 22's setting, the steadiness when having strengthened the support and placing, avoid interchanger body 1 to take place the askew phenomenon of slope.
The above description is only the preferred embodiment of the present invention; the scope of the present invention is not limited thereto. Any person skilled in the art should also be able to cover the technical scope of the present invention by replacing or changing the technical solution and the improvement concept of the present invention with equivalents and modifications within the technical scope of the present invention.
Claims (5)
1. A new high-speed full-chamber resin exchanger, comprising an exchanger body (1), characterized in that: the upper perforated plate (2) is fixedly connected to the upper end inside the exchanger body (1), the middle perforated plate (3) is fixedly connected to the middle position of the exchanger body (1), the lower perforated plate (4) is fixedly connected to the lower end of the exchanger body (1), the upper perforated plate (2) is fixedly connected with a plurality of water feeding caps (5), the middle perforated plate (3) is fixedly connected with a plurality of middle water feeding caps (6), the upper end of the exchanger body (1) is fixedly connected with an upper inlet and outlet (9), the lower end of the exchanger body (1) is fixedly connected with a lower inlet and outlet (10), the upper end of the upper inlet and outlet (9) is fixedly connected with an upper pipeline (11), the upper end of the outer side of the exchanger body (1) is fixedly connected with an upper reinforcing ring (14), and the lower end of the outer side of the exchanger body (1) is fixedly connected with a lower reinforcing ring (15), the lower extreme fixedly connected with a plurality of supporting legs (17) of interchanger body (1), the lower extreme fixedly connected with backup pad (18) of supporting leg (17), a plurality of kicking blocks (19) of lower extreme fixedly connected with of backup pad (18), the lower extreme intermediate position fixedly connected with fore-set (20) of backup pad (18), the lower extreme difference joint of kicking block (19) and fore-set (20) has antiskid cover (21).
2. A novel high speed full compartment resin exchanger as claimed in claim 1 wherein: the lower porous plate (4) is fixedly connected with a plurality of lower water caps (7), and the exchanger body (1) is fixedly connected with a plurality of porous plate supports (8).
3. A novel high speed full compartment resin exchanger as claimed in claim 1 wherein: the lower end of the lower inlet and outlet (10) is fixedly connected with a lower pipeline (12), and one end of the upper pipeline (11) and one end of the lower pipeline (12) are respectively and fixedly connected with a joint (13).
4. A novel high speed full compartment resin exchanger as claimed in claim 1 wherein: the exchanger body (1) is fixedly connected with a plurality of reinforcing ribs (16), and the upper reinforcing ring (14) is fixedly connected with the lower reinforcing ring (15) through the reinforcing ribs (16).
5. A novel high speed full compartment resin exchanger as claimed in claim 1 wherein: the lower end of the anti-skid sleeve (21) is fixedly connected with a plurality of anti-skid blocks (22), and the anti-skid sleeve (21) is made of rubber.
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CN202120704892.9U CN214780913U (en) | 2021-04-07 | 2021-04-07 | Novel high-speed full room resin interchanger |
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CN202120704892.9U CN214780913U (en) | 2021-04-07 | 2021-04-07 | Novel high-speed full room resin interchanger |
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