CN209651983U - A kind of scaling prevention device - Google Patents
A kind of scaling prevention device Download PDFInfo
- Publication number
- CN209651983U CN209651983U CN201920104676.3U CN201920104676U CN209651983U CN 209651983 U CN209651983 U CN 209651983U CN 201920104676 U CN201920104676 U CN 201920104676U CN 209651983 U CN209651983 U CN 209651983U
- Authority
- CN
- China
- Prior art keywords
- cylinder
- water
- new catalytic
- catalytic filler
- prevention device
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
The utility model discloses a kind of scaling prevention devices, including cylinder, quartz sand thickness, new catalytic filler, compression layer and inert layer, the cylinder is vertical cylinder shape stainless steel cylinder, the cylinder upper end is equipped with water outlet, the cylinder lower end is equipped with water inlet, water feed apparatus is fixed with close to described water inlet one end in the cylinder, in the cylinder and it is located at the water feed apparatus equipped with quartz sand thickness, in the cylinder and it is located at the quartz sand thickness equipped with lower partition, in the cylinder and it is located at the lower partition equipped with new catalytic filler, due to water flow dynamic role, free floating state is presented in the new catalytic filler.The utility model has the advantages that the device can convert the easy calcium bicarbonate for forming scale and magnesium bicarbonate to the crystal calcium carbonate and magnesium carbonate of sub-micron, it prevents from forming scale in heat-transfer surface, to improve the heat transfer efficiency of heat exchanger, extend equipment life, and reduce the operating cost of equipment.
Description
Technical field
The utility model relates to field of water treatment equipment, it particularly relates to a kind of scaling prevention device.
Background technique
Currently, in the manufacture course of products of the industries such as chemical industry, pharmacy, papermaking, salt manufacturing, need to carry out water heating or
The calcium bicarbonate or magnesium bicarbonate for being cooled down with water, and being contained in water it is heated or can be changed into after being concentrated calcium carbonate or
Person's magnesium carbonate is precipitated and forms scale and be attached to heat exchanger surface.Scale will lead to the shortening of service life of equipment time and heat exchange effect
Rate reduces, and will increase the operating cost of equipment.
For the problems in the relevant technologies, currently no effective solution has been proposed.
Utility model content
The purpose of this utility model is to provide a kind of scaling prevention devices, to solve mentioned above in the background art ask
Topic.
To achieve the above object, the utility model provides the following technical solutions: a kind of scaling prevention device includes cylinder, quartz
Sand bedding course, new catalytic filler, compression layer and inert layer, the cylinder is vertical cylinder shape stainless steel cylinder, on the cylinder
End is equipped with water outlet, and the cylinder lower end is equipped with water inlet, is fixed with close to described water inlet one end into water in the cylinder
Device, the cylinder is interior and is located at the water feed apparatus equipped with quartz sand thickness, and the cylinder is interior and is located at the quartz sand
Bed course is equipped with lower partition, and the cylinder is interior and is located at the lower partition equipped with new catalytic filler, due to water flow energy
Movement is used, and free floating state is presented in the new catalytic filler, and compression layer is formed at the top of the new catalytic filler, described
It is inert layer in cylinder and on the compression layer, is fixed with water outlet in the cylinder and on the inert layer and fills
Set, the cylinder body outer wall and be located at the inert layer side be equipped with feed inlet, the cylinder body outer wall and be located at the compression layer one
Side is equipped with discharge port, the feed inlet and the discharging equipped with peep-hole, the cylinder body outer wall and positioned at the compression layer side
Mouth has been connected through a screw thread sealing cover.
Further, the new catalytic filler is a kind of active filler, and can be realized will form the calcium bicarbonate of scale
The crystal calcium carbonate and magnesium carbonate of sub-micron are converted into magnesium bicarbonate.
Further, the water inlet is located at cylinder lower end and passes through DN50-DN150 flange or cutting ferrule with the cylinder
Connection, the water feed apparatus are that disc type is intake and is located above water inlet at 0.1-0.5m.
Further, the water outlet in the cylinder upper end and with the cylinder by DN50-DN150 flange or
Cutting ferrule connection, the discharging device are that disc type is discharged and is located at below the water outlet at 0.2-0.5 meters.
Further, the feed inlet is to be connect and be located at 0.1 below the discharging device with the cylinder by flange
The left side of the cylinder at rice.
Further, the peep-hole is to be connect by flange with the cylinder and be located at below the feed inlet 0.3 meter
The left side of the cylinder at place.
Further, the discharge port is connect with the cylinder by flange and is located above water inlet at 0.3-0.8 meters
The cylinder right side.
Compared with prior art, the utility model has the following beneficial effects: the device can be by the easy carbon for forming scale
Sour hydrogen calcium and magnesium bicarbonate are converted into the crystal calcium carbonate and magnesium carbonate of sub-micron, prevent from forming scale in heat-transfer surface, to mention
The heat transfer efficiency of high heat exchanger extends equipment life, and reduces the operating cost of equipment, also has energy conservation, non-scaling, nothing
Disposal of pollutants, filler are configured with compression layer, inert layer, avoid new catalytic filler without cleaning, simple operation and other advantages
Leakage loss.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Needed in attached drawing be briefly described, it should be apparent that, the accompanying drawings in the following description is only the utility model
Some embodiments for those of ordinary skill in the art without creative efforts, can also be according to this
A little attached drawings obtain other attached drawings.
Fig. 1 is the structural schematic diagram according to a kind of scaling prevention device of the utility model embodiment.
Appended drawing reference:
1, cylinder；2, quartz sand thickness；3, new catalytic filler；4, compression layer；5, inert layer；6, water outlet；7, it intakes
Mouthful；8, water feed apparatus；9, peep-hole；10, lower partition；11, feed inlet；12, discharge port；13, discharging device；14, sealing cover.
Specific embodiment
In the following, making further description to utility model in conjunction with attached drawing and specific embodiment:
Embodiment one:
Referring to Fig. 1, according to a kind of scaling prevention device of the utility model embodiment, including cylinder 1, quartz sand thickness 2,
New catalytic filler 3, compression layer 4 and inert layer 5, the cylinder 1 are vertical cylinder shape stainless steel cylinder, 1 upper end of cylinder
Equipped with water outlet 6,1 lower end of cylinder is equipped with water inlet 7, in the cylinder 1 close to described 7 one end of water inlet be fixed with into
Water installations 8, the cylinder 1 is interior and is located at the water feed apparatus 8 equipped with quartz sand thickness 2, and the cylinder 1 is interior and described in
Quartz sand thickness 2 is equipped with lower partition 10, and the cylinder 1 is interior and is located at the lower partition 10 equipped with new catalytic filler
3, due to water flow dynamic role, free floating state, the top of the new catalytic filler 3 is presented in the new catalytic filler 3
Compression layer 4 is formed, the cylinder 1 is interior and is inert layer 5 on the compression layer 4, in the cylinder 1 and is located at the inertia
Discharging device 13 is fixed on layer 5,1 outer wall of cylinder and is located at 5 side of inert layer and is equipped with feed inlet 11, the cylinder
1 outer wall of body and be located at 4 side of compression layer be equipped with peep-hole 9,1 outer wall of cylinder and be located at 4 side of compression layer set
There is discharge port 12, the feed inlet 11 and the discharge port 12 have been connected through a screw thread sealing cover 14.
By the above scheme of the utility model, which can turn the easy calcium bicarbonate for forming scale and magnesium bicarbonate
The crystal calcium carbonate and magnesium carbonate for turning to sub-micron prevent from forming scale in heat-transfer surface, so that the heat transfer efficiency of heat exchanger is improved,
Extend equipment life, and reduce the operating cost of equipment, also has energy conservation, non-scaling, non-pollution discharge, filler without clear
It washes, simple operation and other advantages, is configured with compression layer, inert layer, avoid the leakage loss of new catalytic filler.
Embodiment two:
Referring to Fig. 1, the new catalytic filler 3 is a kind of active filler for new catalytic filler 3, it can
Realize the crystal calcium carbonate and magnesium carbonate for converting the calcium bicarbonate and magnesium bicarbonate that form scale to sub-micron；For water inlet
For 7, the water inlet 7 is located at 1 lower end of cylinder and is connect with the cylinder 1 by DN50-DN150 flange or cutting ferrule, institute
Stating water feed apparatus 8 is that disc type is intake and is located at 7 top 0.1-0.5m of water inlet；For water outlet 6, the water outlet
6 are in 1 upper end of cylinder and are connect with the cylinder 1 by DN50-DN150 flange or cutting ferrule, the discharging device 13
For disc type water outlet and it is located at 6 lower section 0.2-0.5 meters of the water outlet；For feed inlet 11, the feed inlet 11 is
The left side of the cylinder 1 below the discharging device 13 at 0.1 meter is connect and is located at the cylinder 1 by flange；For
For peep-hole 9, the peep-hole 9 is connect and is located at the cylinder 1 by flange at 11 0.3 meter of the lower section of feed inlet
The cylinder 1 left side；For discharge port 12, the discharge port 12 is connect and is located at the cylinder 1 by flange
The right side of the cylinder 1 at top 0.3-0.8 meters of water inlet 7.
In conclusion by means of the above-mentioned technical proposal of the utility model, by setting cylinder 1, quartz sand thickness 2, new
Type catalytic filler 3, compression layer 4 and inert layer 5, when device is run, stoste is intake by water pump from cylinder lower end water inlet 7, is led to
It crosses water feed apparatus 8 and enters quartz sand thickness 2, the suspended matter of larger particles is filtered in quartz sand thickness 2, filtered water passes through
Lower partition 10 enters new catalytic filler 3, and due to water flow dynamic role, free floating state is presented in new catalytic filler 3, and
In the compression layer 4 that float layer top is filler, after inert layer 5 and discharging device 13, water is from 1 upper end water outlet 6 of cylinder
Outflow can be convenient for the situation of the new catalytic filler 3 in observation cylinder 1 by the way that peep-hole 9 is arranged, which can will be easy
The calcium bicarbonate and magnesium bicarbonate that form scale are converted into the crystal calcium carbonate and magnesium carbonate of sub-micron, prevent from being formed in heat-transfer surface
Scale extends equipment life, and reduce the operating cost of equipment to improve the heat transfer efficiency of heat exchanger, also has section
Energy, non-scaling, non-pollution discharge, filler are configured with compression layer, inert layer without cleaning, simple operation and other advantages, avoid new
The leakage loss of type catalytic filler.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (7)
1. a kind of scaling prevention device, which is characterized in that including cylinder (1), quartz sand thickness (2), new catalytic filler (3), pressure
Contracting layer (4) and inert layer (5), the cylinder (1) are vertical cylinder shape stainless steel cylinder, and cylinder (1) upper end is equipped with water outlet
Mouth (6), cylinder (1) lower end are equipped with water inlet (7), are fixed in the cylinder (1) close to the water inlet (7) one end
Water feed apparatus (8), the cylinder (1) is interior and is located at the water feed apparatus (8) equipped with quartz sand thickness (2), the cylinder (1)
It is interior and be located at the quartz sand thickness (2) and be equipped with lower partition (10), in the cylinder (1) and it is located at the lower partition
(10) new catalytic filler (3) are equipped with, due to water flow dynamic role, free floating shape is presented in the new catalytic filler (3)
Compression layer (4) are formed at the top of state, the new catalytic filler (3), in the cylinder (1) and are located on the compression layer (4)
For inert layer (5), the cylinder (1) is interior and is fixed with discharging device (13), the cylinder on the inert layer (5)
(1) outer wall and be located at the inert layer (5) side be equipped with feed inlet (11), cylinder (1) outer wall and be located at the compression layer
(4) side is equipped with discharge port (12) equipped with peep-hole (9), cylinder (1) outer wall and positioned at the compression layer (4) side, institute
It states feed inlet (11) and the discharge port (12) has been connected through a screw thread sealing cover (14).
2. a kind of scaling prevention device according to claim 1, which is characterized in that the new catalytic filler (3) is a kind of
Active filler can be realized crystal calcium carbonate and carbonic acid that the calcium bicarbonate and magnesium bicarbonate that will form scale are converted into sub-micron
Magnesium.
3. a kind of scaling prevention device according to claim 1, which is characterized in that the water inlet (7) is located under cylinder (1)
End and connect with the cylinder (1) by DN50-DN150 flange or cutting ferrule, the water feed apparatus (8) for disc type water inlet and
At 0.1-0.5m above water inlet (7).
4. a kind of scaling prevention device according to claim 1, which is characterized in that the water outlet (6) is in the cylinder
(1) it upper end and is connect with the cylinder (1) by DN50-DN150 flange or cutting ferrule, the discharging device (13) is disc type
It is discharged and is located at below the water outlet (6) at 0.2-0.5 meters.
5. a kind of scaling prevention device according to claim 1, which is characterized in that the feed inlet (11) be by flange with
Cylinder (1) connection and the left side for being located at the cylinder (1) below the discharging device (13) at 0.1 meter.
6. a kind of scaling prevention device according to claim 1, which is characterized in that the peep-hole (9) be by flange with
Cylinder (1) connection and the left side for being located at the cylinder (1) below the feed inlet (11) at 0.3 meter.
7. a kind of scaling prevention device according to claim 1, which is characterized in that the discharge port (12) passes through flange and institute
It states cylinder (1) connection and is located at the right side of the cylinder (1) above water inlet (7) at 0.3-0.8 meters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920104676.3U CN209651983U (en) | 2019-01-22 | 2019-01-22 | A kind of scaling prevention device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920104676.3U CN209651983U (en) | 2019-01-22 | 2019-01-22 | A kind of scaling prevention device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209651983U true CN209651983U (en) | 2019-11-19 |
Family
ID=68521915
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920104676.3U Active CN209651983U (en) | 2019-01-22 | 2019-01-22 | A kind of scaling prevention device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209651983U (en) |
-
2019
- 2019-01-22 CN CN201920104676.3U patent/CN209651983U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103115521B (en) | Device and method for tube type heat exchanger on-line washing | |
| CN109824106A (en) | A kind of continuous seawater desalination system of normal pressure based on hydrate and its application method | |
| CN103977584B (en) | The automatic feed of copper sulphate vacuum evaporator and discharge control method | |
| CN209651983U (en) | A kind of scaling prevention device | |
| CN219024334U (en) | Online cleaning device for ion exchange column | |
| CN202214263U (en) | Drinking water treatment equipment used for stabilizing water quality | |
| CN209500962U (en) | A kind of novel titanium filter | |
| CN207862421U (en) | The primary displacement of zinc powder prepares Spongy Cadmium device | |
| CN2923004Y (en) | Smoke wet-type desulfurizing square absorbing tower | |
| CN106186451A (en) | A kind of processing system containing heavy metal metallurgy waste water | |
| CN205965432U (en) | 4 [ 2 (The acetamido), ethyl ] benzenesulfonyl choride production tail gas HCl absorbing device | |
| CN207375800U (en) | A kind of iron-carbon micro-electrolysis reaction unit | |
| CN206965737U (en) | A kind of aluminium ash prepares flocculant poly aluminium chloride device | |
| CN105582763A (en) | Energy-saving device for non-asbestos silicate board production equipment | |
| CN206253007U (en) | Calcining furnace fume desulfurizing tower bottom slurry disturbance device | |
| CN210874637U (en) | Tail gas treatment device of cold hydrogenation system | |
| CN206204043U (en) | A kind of processing system containing heavy metal metallurgy waste water | |
| CN205061676U (en) | Biological water purification treatment device | |
| CN207487464U (en) | A kind of starch slurry preheating device | |
| CN208814715U (en) | A kind of adaptive hydraulic pressure adjusting water purification filter system | |
| CN215725337U (en) | Metatitanic acid cooling device | |
| CN109821383A (en) | A kind of intelligence prevention and control of air pollution system and method | |
| CN115044732B (en) | Turbidity reducing treatment device of converter dry dedusting coal cold water system | |
| CN216320455U (en) | Gasification black water filter | |
| CN217287190U (en) | Device for reducing concentration, preheating and scaling |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 251604 Liyuan street, economic development zone, Shanghe County, Jinan City, Shandong Province Patentee after: Shandong shuifayou Membrane Technology Co.,Ltd. Address before: 251604 Liyuan street, economic development zone, Shanghe County, Jinan City, Shandong Province Patentee before: Shandong you Film Technology Co.,Ltd. |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: An anti scaling device Effective date of registration: 20221018 Granted publication date: 20191119 Pledgee: Shandong Shanghe Rural Commercial Bank Co.,Ltd. Yuhuangmiao Sub branch Pledgor: Shandong shuifayou Membrane Technology Co.,Ltd. Registration number: Y2022980018831 |