CN106477735A - Water body descaling and antiscaling device and its application - Google Patents
Water body descaling and antiscaling device and its application Download PDFInfo
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- CN106477735A CN106477735A CN201510522619.3A CN201510522619A CN106477735A CN 106477735 A CN106477735 A CN 106477735A CN 201510522619 A CN201510522619 A CN 201510522619A CN 106477735 A CN106477735 A CN 106477735A
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- water body
- antiscaling
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- water
- descaling
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Abstract
The invention discloses a kind of water body antiscaling and descaling device, including:It is arranged on water body and flows through the tubular shell on pipeline;And coaxial fixation is set in the core in housing, its outer surface setting is fluted, and the space which is formed between inner walls is used as the runner of water body flow;The flow passage structure of core can be contacted with core when water can be caused to flow wherein and rub and produced vortex by certain shock, so as to combining discrete for the metal electron in alloy release with calcium ions and magnesium ions absorption in water, realize the antiscaling, descaling to water body.The invention also discloses its application in heat exchanger antiscaling, descaling.Assembly of the invention can realize the effective descaling and antiscaling to water body, solve the technical problem that efficiency is low, tartar preventing iron tartar effect is poor in current device.
Description
Technical field
The invention belongs to water-treatment technology field, and in particular to a kind of water body antiscaling and descaling device and its application.
Background technology
In boiler, cooling tower, heat exchanger and nearly all application for utilizing water to be heated or cooled, fouling
(with calcium carbonate and other mineral forms) are all subject matters.In industrial processes, because water is cheap
And be readily available, water is often used as the carrier of heat transfer.The heat produced in production process passes through a heat
Switch (heat exchanger, condenser etc.) is transferred in cooling water, is then evaporated in cooling tower by water
And distribute heat in nature.The original water in poised state, changes condition in heat-exchanger surface,
Crystallization deposition is easy to, becomes incrustation scale, become industrial harm.
First, incrustation scale is heat-insulated, can reduce heat exchange coefficient, can so increase extra energy ezpenditure;Its
Secondary, incrustation scale meeting blocking heat-exchanger, refrigerator, pump, pipeline and valve, so as to increase pressure, the minimizing of water
The flow of water, cause leakage, even cause thoroughly irremediable damage;In addition, incrustation scale is carried to microorganism
For protection, the hotbed of breeding is provided to microorganism, causes biological pollution and underdeposit corrosion.
The prevention of incrustation scale and removing become the technical problem that must be faced and solve.Process currently for incrustation scale
It is all generally the processing mode combined using antiscale and scale removal, mainly chemical method and two class of physical method.Often
The chemical treatments that sees are mainly and add chemicals in water body, are realized to incrustation scale using chemical reaction mode
Elimination or prevent in pre- waterproof body calcium and magnesium particle to generate corresponding incrustation scale material.But, chemical method one is
Impact of extra these chemical substances that adds to water body or environment, two is that its price is high, causes industrial cost
Notable rising;Three is that elimination effect is also limited, remains a need for further cleaning in many cases.
Physical method generally includes mechanical cleaning mode or by the way of water body filtration.Mechanical cleaning is generally needed
Carry out after shutting down, reduce production efficiency, and cleaning performance have to be strengthened;Prevented by way of filtering
Most of calcium and magnesium particle can be effectively filtered in dirty scale removal, but, as filter core needs periodic replacement so that
Actual cost is greatly promoted, and is filtered or delayed water velocity, causes time formation efficiency to reduce.
At present, occur in that carries out the technical scheme of antiscaling, descaling using ultrasonic wave or magnetic means, i.e., using ultrasound
The mode of ripple is processed to incrustation scale, is removed incrustation scale or is delayed the generation of incrustation scale, or utilizes magnetic fields by water
Calcium ions and magnesium ions in body are magnetized, so as to prevent fouling.Above-mentioned technological means can preferably be realized antiscale and remove
Dirt, but the ultrasonic unit due to needing additional special and magnetizing assembly so that equipment overall structure is multiple
Miscellaneous, it is not suitable for commercial Application is needed, and cost can be increased, in addition ultrasonic wave or magnetization can be to water body or rings
Border can produce certain impact so which is using being restricted.
A kind of descaling and antiscaling device is disclosed in Chinese patent literature CN201320794373.1, and the device is outside
Spiral alloy sheet is installed inside shell, crust of the device two ends are connected with inlet channel by joint, and the spiral is closed
Gold plaque adopts the fluid origin plate shape of high potential metal alloy, then cuts into sheet, then turns round along long axis centerline
Three-sixth turn curl.When current are through spiral alloy sheet, each molecule in water is in the mistake of helical flow
Contact with spiral alloy sheet in journey, when contact, high rest potential spiral alloy sheet is connect with the calcium ion in water
Touch and potential difference is produced, the potential difference acts on calcium ion so as to generation calcium carbonate smoothly can not be combined with carbonate
Precipitation fouling, realizes the purpose of good antiscale property and scale removal.The device can in the case of impact production is avoided as far as possible,
Using alloy and the effect of calcium ion in water body, so as to prevent the generation of incrustation scale, imitate with preferable antiscaling, descaling
Really.But, the device yet suffers from following problem:1) impact of the spiral alloy chip architecture to current,
I.e. the alloy sheet reverses shaping by tabular, and which has certain impact as water stream channel to water body flow speed,
Efficiency is caused to reduce;2) flow passage structure of alloy sheet cannot ensure that each molecule in water can be connect with alloy sheet
Touch, so as to antiscale and scale removal effect can be caused to be affected;3) fail in the device to alloy sheet composition and its
Component is defined, and Conventional alloys are general with hydrone action effect, and therefore the device is to the actual scale removal of water body
Antiscaling effect is also to be hoisted.
Content of the invention
Disadvantages described above or Improvement requirement for prior art, the invention provides a kind of water body antiscaling and descaling device
And its application, which passes through to arrange antiscaling and descaling device on water body flow pipeline, arranges with optimizing flow passage in which
The spiral alloy core of structure, so as to realize the effective descaling and antiscaling to water body, solves efficiency in current device
The poor technical problem of low, tartar preventing iron tartar effect.
For achieving the above object, according to one aspect of the present invention, a kind of water body antiscaling and descaling device is provided, its
It is arranged on water body flow pipeline, for realizing the antiscaling, descaling to water body, wherein, the device includes:Arrange
The tubular shell on pipeline is flowed through in water body;And coaxial fixation is set in the core in housing, its outer surface
Setting is fluted, and the space which is formed between inner walls is used as the runner of water body flow;
Characterized in that, the flow passage structure of the core can cause water contact with core when flowing wherein rubbing
Wipe and simultaneously produced vortex by certain shock, so as to can by discrete for the metal electron in alloy release with water in
Calcium ions and magnesium ions absorption is combined, and realizes the antiscaling, descaling to water body.Wherein current Reynolds number is in (30000,80000)
In the range of, i.e., 30000<(Re=ρ vd/ η)<80000, preferably in the range of (40000,70000),
Wherein v, ρ, η are respectively flow velocity, density and the viscosity of fluid, and d is pipe diameter.
Used as the improvement of the present invention, the core is made up of alloy material, alloying component be preferably copper, zinc, lead,
Nickel, while comprising micro aluminium, iron, manganese and/or silver.
Used as the improvement of the present invention, the alloying component mass percentage content is preferably copper 40%-60%, zinc
15%-25%, lead 4%-8%, nickel 15%-25%, more preferably copper 50-55%, zinc 18%-22%, 4%-6%,
Nickel 18%-23%, most preferably copper 50%, zinc 20%, lead 5%, nickel 20%.
Used as the improvement of the present invention, the mass percentage content of the trace meter such as the aluminium, iron, manganese, silver is preferred
For 0.1-2% scope.
Used as the improvement of the present invention, the helically type of the runner in the core, the helical angle of helix are generally higher than
45 °, preferably greater than 55 °, particularly preferably 60-70 °.
Used as the improvement of the present invention, the runner in the core is dug along water (flow) direction in core outer surface
The part that does not dig on groove, and core surfaces becomes multiple projections, each raised in streamline in water (flow) direction
Type structure.
Used as the improvement of the present invention, the recess width is preferably 0.05-0.2 times of core diameter, more preferably
0.1 to 0.15 times,
It is another aspect of this invention to provide that providing a kind of using above-mentioned water body antiscaling and descaling device in boiler or heat exchange
Application in device.
Assembly of the invention considers the potential difference between pipeline metal itself and scale removal alloy, employs ground connection
, with more the generality of commercial Application, there is the substantially former of galvanic interaction based on metal potential difference in safeguard measure
Reason, the reasonable combination with structure design so that product can accurate Quantitative design, can be applicable to all size
In the pipeline of flow velocity.Non-maintaining, installation is simple, and without the need for extra power supply and chemicals, shelf life can
Reach more than 15 years.
In general, by the contemplated above technical scheme of the present invention compared with prior art, have with following
Beneficial effect:
(1) alloy core in apparatus of the present invention adopts setting for the flow passage structure of optimization design, its size and radian
Meter allows water body to reach when flowing through when flow area is maximum and keeps flow resistance minimum, so as to effectively reduce current
Impact of the speed to production efficiency;
(2) alloy core in apparatus of the present invention can be protected when water body is flowed through using the flow passage structure of optimization design
The water that flows through of card all can carry out CONTACT WITH FRICTION with alloy core and produce vortex, so as to realize alloy and water from
Son absorption, effectively realizes antiscaling, descaling;
(3) in apparatus of the present invention core alloying component using copper, silver, lead and zinc and trace element combination and
Composition, can ionize so that it can maximizing under vortex impact, the grounding shell with alloy material
Between produce autonomous potential, calcium ions and magnesium ions effectively therein can not be deposited and fouling in this role, be realized effectively
Antiscaling, descaling;
(4) assembly of the invention can realize the effective descaling and antiscaling to water body, and which is without the need for shutdown, efficiency
Height, while production cost ground, affecting on water body and environment nothing, tartar preventing iron tartar effect is good.
Description of the drawings
Fig. 1 is the structural representation of the water body antiscaling and descaling device according to one embodiment of the invention;
Fig. 2 is the structural representation of the core of the water body antiscaling and descaling device according to one embodiment of the invention;
Fig. 3 is the application schematic diagram of the water body antiscaling and descaling device according to one embodiment of the invention.
Specific embodiment
In order that the objects, technical solutions and advantages of the present invention become more apparent, below in conjunction with accompanying drawing and enforcement
Example, the present invention will be described in further detail.It should be appreciated that specific embodiment described herein is only used
To explain the present invention, it is not intended to limit the present invention.Additionally, each embodiment of invention described below
As long as in involved technical characteristic do not constitute conflict each other and can just be mutually combined.
According to a kind of water body antiscaling and descaling device constructed by the embodiment of the present invention, as shown in figure 1, including flange
1st, shell 2, core 3, flange 4 and fixed mount 5.
Wherein, shell 2 is constituted by two sections, and both are coaxially fixing and with bolts by the flange 4 of end,
To form barrel type shell mechanism, shell 2 is preferably alloy by metal and makes.
The each section of relative other end of shell is also equipped with flange 1, for being connected with external water pipe, so as to should
Antiscaling and descaling device is on pipeline.
Core 3 is preferably coaxially fixed on housing 2 by fixing in the cavity inside the housing of fixed mount 5
Central axis on.Water flow through after entering shell 2 core 3 with spiral flow channel from another side flange stream to
Docking pipeline, so as to carry out antiscaling, descaling to water body.
Core 3 is the core component of this device, and which is the crucial portion that this device is achieved its antiscaling, descaling function
Part.Core 3 is made up of alloy material, and during with appropriate water impact, the metallic element as anode can be in water
Electronics is lost under effect, the impact under certain flow rate causes debunching in water, so as to calcium and magnesium in water from
There is suction-operated in son so that ion volume becomes big, it is difficult to become incrustation scale deposition.Specifically, when water flows through conjunction
During golden kernel, the potential difference between alloying element causes anode metal to discharge a large amount of free electrons, and these are freely electric
Son occurs electrode reaction to form stable state with Ca2+, Mg2+ ion in hard water, in preventing which with water
Oxide compound generates rust and incrustation scale.While free electron occurs electrode reaction to be formed with Fe2+ and Fe3+ ion
Stable state, reduces water iron-holder.
In the present embodiment, the alloy material composition of core be preferably the bulk composition such as copper zinc lead nickel and including aluminium,
The trace elements such as iron, manganese, silver, usually, in order to more effectively water impact effect under discharge electronics with from
It is scattered in water, each Ingredient percent content is preferably controlled in copper 40%-60%, zinc 15%-25%, lead
4%-8%, nickel 15%-25%, more preferably copper 50-55%, zinc 18%-22%, 4%-6%, nickel 18%-23%,
Most preferably copper 50%, zinc 20%, lead 5%, nickel 20%, the trace meter such as remaining aluminium, iron, manganese, silver
Content specifically can be determined according to actual needs, for example accounted in the range of 0.1-2% respectively.
In the composition of alloying component, metallic copper is low price and the material that is readily available, zinc in precious metal material
The addition of metal can have larger potential difference with reduces cost and between metallic copper, however, to ensure that core
The toughness of the heart sets upper content limit as 20%, add tin be in order to put forward heavy alloyed corrosion resistance and intensity, add micro-
Amount silver can play the role of sterilization algae removal, and other trace meters are all for the needs of smelting process.Above-mentioned alloy becomes
Divide and its content, the water of flowing can be caused when core is washed away, which has the electronics releasability of maximum and work
Change energy, while its reaction that can realize maximum being formed with the calcium and magnesium plasma in water is inhaled according to galvanic principles
Attached effect, realizes the generation of incrustation scale so as to maximizing.Alloy core and the galvanic cell of metal shell (ground connection)
Reaction can occur anode loss protection reaction to the carbon steel piping for connecting, so as to realize the effect of antirust, anti-corrosive.
It is in axis structure that core 3 is overall, and its periphery offers the runner logical for current, the runner of periphery
Can be spirality, streamlined or other kinds of flow passage structure.3 surface flow passage structure of core is impact antiscale
Another key factor of scale removal effect, is to improve tartar preventing iron tartar effect, should ensure that the water body for flowing through can be maximum
Contact with core to degree so as to wash away alloy core 3, while should ensure that flow passage resistance force of waterproof is minimum as much as possible,
Reduce the impact to current sales volume.The flow passage structure of this device should ensure that the Reynolds number of current (30000,
80000) in the range of, i.e., 30000<(Re=ρ vd/ η)<80000, water is in such runner within the range
Can be subject to certain shock produce vortex during middle flowing, so as to will discrete for the metal electron in alloy so as to and water
Middle calcium ions and magnesium ions etc. are combined, and in the present embodiment preferably in the range of (40000,70000), its adsorption effect is most
Good.Wherein, v, ρ, η are respectively flow velocity, density and the viscosity of fluid, and d is pipe diameter.
Runner in this device core 3 is in one embodiment for being arranged on core outer surface twist
Groove, recess width is preferably 0.05-0.2 times of core diameter, more preferably 0.1 to 0.15 times, spiral
Generally higher than 45 °, preferably greater than 55 °, particularly preferably 60-70 ° of the helical angle of line.Above-mentioned size and
The design of angle, can enable water body swimmingly to flow through core surfaces, and can be subject to certain shock with
Vortex is produced, so as to will be discrete for the metal electron in alloy to combine with calcium ions and magnesium ions in water etc..Above-mentioned groove
The concrete numerical value of width and helical angle can carry out specifically chosen setting according to current actual flow velocity in pipeline.
In an alternative embodiment of the invention, the runner in core 3 is opened along water (flow) direction in core outer surface
The groove of chisel, and cause the part that does not dig in core surfaces to become multiple projections, each projection is along water (flow) direction
Upper streamlined structure so that current can flow through each projection naturally, and thereby circulate from core surfaces, while
Vortex can be excited, will be discrete for the metal electron in alloy to combine with calcium ions and magnesium ions in water etc..
In the device, the major function of the structure of runner is the work for reducing particulate in flow resistance and discretization water
With.Which ensures that the logical area of current is approximate with connecting pipe first, while avoiding excessively producing local pressure loss
Structure, the such as not excessive fluidal texture of design area difference, do not design especially less than 90 degree of bend
Curved channel;Secondly, in the present embodiment, can be by the emulation of CFD under nominal flow rate, its flow passage structure makes
Obtain water is subject to certain shock generation to be vortexed in flowing, so as to will be discrete for the metal electron in alloy, brings water into
In, so as to there is suction-operated with calcium ions and magnesium ions in water so that ion volume becomes big, it is difficult to become incrustation scale deposition.
The flow passage structure of apparatus of the present invention, can be with comprehensive reducing slight drag and the feature of the vortex for producing discretization electronics, its
Optimal tartar preventing iron tartar effect can be obtained under conditions of flow resistance is reduced as far as possible.
Assembly of the invention is due between the internal alloy core 3 with activation evergy and the shell 2 of alloy material
Autonomous potential is produced, as the alloy core 3 of activation evergy is with lasting ionizability, while core 3
Special construction constantly produce a large amount of electronics with the water friction that flows through, can prevent and eliminate the iron of generation in pipeline
Rust and dirt, while the diaphragm of similar a layer thickness can also be formed in inner-walls of duct, prevent the generation of iron rust.
According to specifically used environment, the descaling water pipe equipment of the present invention can make different-diameter according to line size
The flange of (such as 15mm~300mm), need not consume electric energy, Maintenance free, and the life-span was up to 20 years.
Assembly of the invention can be applied in the antiscaling, descaling in the fields such as heat exchanger, boiler or pipeline.
For example in heat exchanger, as the incrustation scale of heat exchanger is primarily generated in the pipeline of heat exchange concentration, once produce water
Dirt has a strong impact on heat transfer effect and safe operation.Apparatus for eliminating sludge is directly installed in series heat exchanger circulation
In pipeline, the position that can arbitrarily be easily installed.After installation, any original water circulation work is not being affected
In the case of condition, in the heat exchange surface of heat exchanger and heat exchange pipeline, any incrustation scale is not produced, if originally
There is outmoded incrustation scale, after the heat exchanger equipped with apparatus for eliminating sludge runs three months, incrustation scale is eliminated.
As it will be easily appreciated by one skilled in the art that presently preferred embodiments of the present invention is the foregoing is only, not
In order to limit the present invention, all any modifications that is made within the spirit and principles in the present invention, equivalent and change
Enter, should be included within the scope of the present invention.
Claims (9)
1. a kind of water body antiscaling and descaling device, which is arranged on water body flow pipeline, and for realizing the antiscaling, descaling to water body, wherein, the device includes:It is arranged on water body and flows through the tubular shell on pipeline;And coaxial fixation is set in the core in housing, its outer surface setting is fluted, and the space which is formed between inner walls is used as the runner of water body flow;
It is characterized in that, the flow passage structure of the core can be contacted with core when water can be caused to flow wherein and rub and produced by certain shock vortex, so as to combining discrete for the metal electron in alloy release with calcium ions and magnesium ions absorption in water, the antiscaling, descaling to water body is realized.
2. a kind of water body antiscaling and descaling device according to claim 1, wherein, flows through the current Reynolds number of core in the range of (30000,80000), i.e., and 30000<(Re=ρ vd/ η)<80000, preferably in the range of (40000,70000), wherein v, ρ, η are respectively flow velocity, density and the viscosity of fluid, and d is pipe diameter.
3. a kind of water body antiscaling and descaling device according to claim 1 and 2, wherein, the core is made up of alloy material, and alloying component is preferably copper, zinc, lead, nickel, while comprising micro aluminium, iron, manganese and/or silver.
4. a kind of water body antiscaling and descaling device according to claim 3, wherein, the alloying component mass percentage content is preferably copper 40%-60%, zinc 15%-25%, lead 4%-8%, nickel 15%-25%, more preferably copper 50-55%, zinc 18%-22%, 4%-6%, nickel 18%-23%, most preferably copper 50%, zinc 20%, lead 5%, nickel 20%.
5. a kind of water body antiscaling and descaling device according to claim 3 or 4, wherein, the mass percentage content of the trace meter such as the aluminium, iron, manganese, silver is preferably 0.1-2% scope.
6. a kind of water body antiscaling and descaling device according to any one of claim 1-5, wherein, runner in the core helically type, generally higher than 45 °, preferably greater than 55 °, particularly preferably 60-70 ° of the helical angle of helix.
7. a kind of water body antiscaling and descaling device according to any one of claim 1-6, wherein, runner in the core is the groove that digs along water (flow) direction in core outer surface, and the part that does not dig in core surfaces becomes multiple projections, and each projection is in streamlined structure in water (flow) direction.
8. a kind of water body antiscaling and descaling device according to any one of claim 1-7, wherein, the recess width is preferably 0.05-0.2 times, more preferably 0.1 to 0.15 times of core diameter.
9. application of the water body antiscaling and descaling device any one of claim 1-8 in boiler or heat exchanger.
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107226535A (en) * | 2017-07-14 | 2017-10-03 | 南京超旭节能科技有限公司 | Complete intelligent water purification scale prevention device on heat exchange manifold |
CN107365922A (en) * | 2017-07-14 | 2017-11-21 | 南京超旭节能科技有限公司 | Full intelligent ground descaling device |
CN107555618A (en) * | 2017-07-20 | 2018-01-09 | 亚华美(北京)环境科技发展有限公司 | A kind of water pipe rust removing and contaminant releasing and anti-corrosion device |
CN109763018A (en) * | 2019-02-25 | 2019-05-17 | 武汉众胜斯特科技有限公司 | A kind of descaling and antiscaling alloy, descaler and preparation method thereof |
CN110240295A (en) * | 2019-06-03 | 2019-09-17 | 常州大学 | Graphene scaling prevention device |
CN110407393A (en) * | 2019-07-12 | 2019-11-05 | 翱途能源科技(无锡)有限公司 | Microscale-electronic descaling and antiscaling instrument |
CN112197100A (en) * | 2020-10-25 | 2021-01-08 | 台州半城暖通科技有限公司 | Pipeline anti-scaling device |
CN113697969A (en) * | 2021-09-02 | 2021-11-26 | 中国石油化工股份有限公司 | Alloy anti-scaling device for salt-containing sewage scale prevention |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2127581A (en) * | 1982-09-07 | 1984-04-11 | Raymond G Gauger | Apparatus for preventing scale formation in water systems |
CN1982227A (en) * | 2005-12-15 | 2007-06-20 | 唐辉 | Ionic rod water treater in water pool |
CN103274493A (en) * | 2013-06-19 | 2013-09-04 | 王斌 | Pipeline descaling device |
CN103896411A (en) * | 2014-03-12 | 2014-07-02 | 河北工业大学 | Water treatment core component and water treatment device |
-
2015
- 2015-08-24 CN CN201510522619.3A patent/CN106477735A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2127581A (en) * | 1982-09-07 | 1984-04-11 | Raymond G Gauger | Apparatus for preventing scale formation in water systems |
CN1982227A (en) * | 2005-12-15 | 2007-06-20 | 唐辉 | Ionic rod water treater in water pool |
CN103274493A (en) * | 2013-06-19 | 2013-09-04 | 王斌 | Pipeline descaling device |
CN103896411A (en) * | 2014-03-12 | 2014-07-02 | 河北工业大学 | Water treatment core component and water treatment device |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107226535A (en) * | 2017-07-14 | 2017-10-03 | 南京超旭节能科技有限公司 | Complete intelligent water purification scale prevention device on heat exchange manifold |
CN107365922A (en) * | 2017-07-14 | 2017-11-21 | 南京超旭节能科技有限公司 | Full intelligent ground descaling device |
CN107555618A (en) * | 2017-07-20 | 2018-01-09 | 亚华美(北京)环境科技发展有限公司 | A kind of water pipe rust removing and contaminant releasing and anti-corrosion device |
CN109763018A (en) * | 2019-02-25 | 2019-05-17 | 武汉众胜斯特科技有限公司 | A kind of descaling and antiscaling alloy, descaler and preparation method thereof |
CN110240295A (en) * | 2019-06-03 | 2019-09-17 | 常州大学 | Graphene scaling prevention device |
CN110407393A (en) * | 2019-07-12 | 2019-11-05 | 翱途能源科技(无锡)有限公司 | Microscale-electronic descaling and antiscaling instrument |
CN112197100A (en) * | 2020-10-25 | 2021-01-08 | 台州半城暖通科技有限公司 | Pipeline anti-scaling device |
CN113697969A (en) * | 2021-09-02 | 2021-11-26 | 中国石油化工股份有限公司 | Alloy anti-scaling device for salt-containing sewage scale prevention |
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