CN112340256A - Magnesium hydroxide slurry supply device and application thereof - Google Patents
Magnesium hydroxide slurry supply device and application thereof Download PDFInfo
- Publication number
- CN112340256A CN112340256A CN202011345735.XA CN202011345735A CN112340256A CN 112340256 A CN112340256 A CN 112340256A CN 202011345735 A CN202011345735 A CN 202011345735A CN 112340256 A CN112340256 A CN 112340256A
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- Prior art keywords
- slurry
- storage tank
- magnesium hydroxide
- pipeline
- slurry supply
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Links
- 239000002002 slurry Substances 0.000 title claims abstract description 89
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 title claims abstract description 33
- 239000000347 magnesium hydroxide Substances 0.000 title claims abstract description 30
- 229910001862 magnesium hydroxide Inorganic materials 0.000 title claims abstract description 30
- 230000001105 regulatory effect Effects 0.000 claims abstract description 14
- 238000006477 desulfuration reaction Methods 0.000 claims abstract description 11
- 230000023556 desulfurization Effects 0.000 claims abstract description 11
- 238000011010 flushing procedure Methods 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims description 11
- 230000003009 desulfurizing effect Effects 0.000 claims description 11
- 238000005406 washing Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 230000001276 controlling effect Effects 0.000 claims description 4
- 238000000151 deposition Methods 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 4
- 230000008878 coupling Effects 0.000 claims description 3
- 238000010168 coupling process Methods 0.000 claims description 3
- 238000005859 coupling reaction Methods 0.000 claims description 3
- 238000001704 evaporation Methods 0.000 claims description 3
- 230000008020 evaporation Effects 0.000 claims description 3
- 239000013072 incoming material Substances 0.000 claims description 3
- 238000001556 precipitation Methods 0.000 claims description 2
- 238000003756 stirring Methods 0.000 abstract description 4
- 230000009471 action Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D88/00—Large containers
- B65D88/54—Large containers characterised by means facilitating filling or emptying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/53—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is discharged from and reintroduced into a receptacle through a recirculation tube, into which an additional component is introduced
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/80—Forming a predetermined ratio of the substances to be mixed
- B01F35/83—Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
- B01F35/833—Flow control by valves, e.g. opening intermittently
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D88/00—Large containers
- B65D88/74—Large containers having means for heating, cooling, aerating or other conditioning of contents
- B65D88/744—Large containers having means for heating, cooling, aerating or other conditioning of contents heating or cooling through the walls or internal parts of the container, e.g. circulation of fluid inside the walls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D90/00—Component parts, details or accessories for large containers
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a magnesium hydroxide slurry supply device and application thereof, and the device comprises a storage tank, wherein a discharge valve penetrates through the side wall of the storage tank, the discharge valve is connected with a desulfurization tower slurry pool through a guide pipe, a feed pump is arranged on the discharge valve, one end of a loop pipeline is connected to the guide pipe through a first type connector, the other end of the loop pipeline is connected with the storage tank, and a flow regulating valve is arranged on the guide pipe between the desulfurization tower slurry pool and the first type connector, so that a part of slurry can flow into the storage tank again along with the loop pipeline under the action of the flow regulating valve, and the slurry is kept circulating in the pipeline all the time, and is prevented from being deposited in the pipeline; the conventional stirring and dispersing device is not needed, the slurry in the storage tank is disturbed by the backflow slurry, and the slurry in the tank body is prevented from being deposited; the stable and reliable supply of the magnesium hydroxide slurry is realized.
Description
Technical Field
The invention relates to the technical field of slurry supply, in particular to a magnesium hydroxide slurry supply device and application thereof.
Background
The magnesium flue gas desulfurization process is being regarded by people and gradually developed into the mainstream flue gas desulfurization technology. The desulfurizer is usually magnesium oxide or magnesium hydroxide powder, water is added to prepare slurry before use, the operation process is complicated, dust pollution often exists in the use field, and the health of workers is affected. In order to reduce the operation links and facilitate the feeding of the desulfurizer, the magnesium hydroxide is expected to be in a slurry form so as to facilitate the long-term storage, transportation and pumping of the magnesium hydroxide. The desulfurizing agent for magnesium hydroxide slurry is a novel product, and if a user is not familiar with the characteristics of slurry and unique handling characteristics, improper procedures may cause unnecessary troubles. Slurries are suspensions of fine solids that can result in plugging and solids accumulation problems due to poor mixing, improper piping and/or improper pump selection.
Disclosure of Invention
The present invention is directed to a magnesium hydroxide slurry supply device and an application thereof to solve the above problems of the related art.
In order to achieve the purpose, the invention provides the following technical scheme: the utility model provides a magnesium hydrate thick liquids feeding device, includes the storage tank, the lateral wall of storage tank runs through and is equipped with the bleeder valve, the bleeder valve has desulfurizing tower thick liquids pond through pipe connection, be equipped with the feed pump on the bleeder valve, be connected with the one end of return circuit pipeline through first type connector on the pipe, the other end of return circuit pipeline with the storage tank is connected, correspond on the pipe desulfurizing tower thick liquids pond with be equipped with flow control valve between the first type connector.
Preferably, the loop pipeline is positioned on the side wall of the storage tank corresponding to the lower end of the discharge valve.
Preferably, the lower end of the inner surface of the storage tank is fixedly connected with a flexible disturbance belt.
Preferably, the device also comprises a flushing pipeline, a flushing water pump is arranged on the flushing pipeline, a cooling nozzle penetrates through the upper side wall of the storage tank, and the flushing pipeline is connected with the cooling nozzle pipe.
Preferably, a second T-shaped connector is arranged on the catheter, and the flushing pipeline is connected with the second T-shaped connector respectively.
Preferably, the flushing pipeline inlets are generally two, and are respectively arranged before the feeding pump and after the feeding pump, so that when the system stops running for a long time, the feeding pump and the slurry in the pipeline are flushed clean, and the slurry is prevented from depositing in the pipeline and the feeding pump.
Preferably, the flexible disturbance zone is provided with a plurality of openings, the diameter of each opening is determined according to the backflow flow, and the flow speed of the backflow slurry flowing through each opening is preferably more than 1 m/s.
Preferably, the openings arranged on the flexible disturbance band are distributed in a downward cross mode and are used for flushing and disturbing deposited slurry at the bottom of the tank so as to prevent hard sedimentation.
Preferably, the feed pump type is one of a diaphragm pump, a slurry pump or a screw pump.
Another aspect of the present invention provides a use of the magnesium hydroxide slurry supply apparatus, comprising:
firstly, incoming materials enter a storage tank through a feeding hole on the storage tank to be stored for later use;
secondly, when the system runs, a discharge valve and a feed pump are opened, the flow is regulated and controlled by controlling a flow regulating valve, redundant slurry flows back to the tank bottom flexible disturbance pipe belt through a first T-shaped connector, the pipe belt fluctuation is caused when the backflow slurry flows in the tank bottom flexible disturbance pipe belt, and the effect of preventing the sedimentation of the disturbance slurry is achieved;
thirdly, keeping the flow velocity of the slurry in the pipeline not higher than 5m/s during operation; more preferably the speed is 2 m/s;
and fourthly, when the magnesium hydroxide slurry supply device is stopped, starting a washing water pump to wash the slurry inside the pipeline to prevent the slurry from depositing in the pipeline.
Preferably, in the technical solution of the application of the above magnesium hydroxide slurry supply device, the magnesium hydroxide slurry supply device is further connected to a desulfurization tower, and the desulfurization tower is provided with a slurry pool; and the flow regulation and control step is to regulate and control the flow of the magnesium hydroxide slurry supply device flowing into the slurry pool of the desulfurization tower.
Preferably, in the technical scheme of the application of the magnesium hydroxide slurry supply device, when the ambient temperature is higher than 40 ℃, the rinse water pump is periodically started, and the slurry in the storage tank is cooled through the cooling nozzle and the evaporation loss water is replenished.
Compared with the prior art, the invention has the beneficial effects that: a magnesium hydroxide slurry supply device is provided with a loop pipeline and a flow regulating valve on the pipeline, so that a part of slurry can flow into a storage tank again along with the loop pipeline under the action of the flow regulating valve, the slurry is always circulated in the pipeline, and the slurry is prevented from being deposited in the pipeline; the conventional stirring and dispersing device is not needed, the slurry in the storage tank is disturbed by the backflow slurry, and the slurry in the tank body is prevented from being deposited; the stable and reliable supply of the magnesium hydroxide slurry is realized.
Drawings
Fig. 1 is a schematic front view of the present invention.
In the figure: 1-a material storage tank, 2-a discharge valve, 3-a desulfurizing tower slurry pool, 4-a feeding pump, 5-a first T-shaped connector, 6-a loop pipeline, 7-a flow regulating valve, 8-a flexible disturbance belt, 9-a flushing pipeline, 10-a cooling nozzle and 11-a second T-shaped connector.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1
Referring to fig. 1, the present invention provides a technical solution: the utility model provides a magnesium hydrate thick liquids feeding device, includes storage tank 1, the lateral wall of storage tank 1 runs through and is equipped with bleeder valve 2, bleeder valve 2 has desulfurizing tower thick liquids pond 3 through pipe connection, be equipped with feed pump 4 on bleeder valve 2, feed pump 4 opens, goes into desulfurizing tower thick liquids pond 3 with the built-in thick liquids of storage tank 1 through the pipe pump, be connected with the one end of return circuit pipeline 6 through first T type connector 5 on the pipe, the other end of return circuit pipeline 6 with storage tank 1 is connected, correspond on the pipe desulfurizing tower thick liquids pond 3 with be equipped with flow control valve 7 between first T type connector 5.
Specifically, the loop pipe 6 is located on the sidewall of the storage tank 1 corresponding to the lower end of the discharge valve 2.
Particularly, the internal surface lower extreme fixedly connected with flexible disturbance area 8 of storage tank 1 is injected into by the lower extreme through return circuit pipeline 6 the inside thick liquids of storage tank 1 wash flexible disturbance area 8 for flexible disturbance area 8 constantly turns over the hank under this effect, stirs the thick liquids in the storage tank 1, avoids the thick liquids deposit on the lateral wall of storage tank 1.
Particularly, still including flushing pipe 9, be equipped with washing water pump on the flushing pipe 9, through washing water pump to the inside water injection of flushing pipe 9, the last lateral wall of storage tank 1 runs through and is equipped with cooling nozzle 10, flushing pipe 9 with cooling nozzle 10 union coupling, the water in the flushing pipe 9 passes through cooling nozzle 10 and sprays in storage tank 1's inside, washs storage tank 1.
Particularly, be equipped with a plurality of second T type connector 11 on the pipe, wash pipeline 9 respectively with 11 union couplings of second T type connector, wash pipeline 9 corresponds second T type connector 11 punishment is equipped with the valve respectively for control wash opening and shutting of pipeline 9 to wash in the pipe, reach abluent mesh.
Specifically, the flexible disturbance belt 8 is provided with a plurality of openings, the diameter of each opening is determined according to the backflow flow, the flow speed of backflow slurry flowing through the opening is preferably larger than 1m/s, and the openings in the flexible disturbance belt 8 can reduce the resistance of the flexible disturbance belt 8 to the backflow slurry when the flexible disturbance belt 8 moves, so that the stirring efficiency of the flexible disturbance belt 8 to the slurry in the discharge pipe 1 is improved.
In particular, the feed pump 4 is of the type of a diaphragm pump, a slurry pump or a screw pump.
The working principle is as follows: when the device is used, slurry is in the discharging pipe 1, enters the guide pipe through the discharging valve 2, finally flows into the slurry pool 3 of the desulfurizing tower, and the flow velocity of the slurry flowing through the flow regulating valve 7 is controlled through the flow regulating valve 7, so that redundant slurry enters the loop pipeline 6 through the first T-shaped connector 5 and then flows into the storage tank 1, the flow of the slurry is kept, and meanwhile, the slurry in the storage tank 1 is stirred.
Example 2
The embodiment relates to an application of the invention, which comprises the following steps:
firstly, the incoming material enters the material storage tank 1 through the material inlet on the material storage tank 1 to be stored for standby,
secondly, opening a discharge valve 2 and a feed pump 4 when the system operates, regulating and controlling the flow flowing into a slurry pool of the desulfurization tower by controlling a flow regulating valve 7, wherein redundant slurry flows back to a tank bottom flexible disturbance pipe belt 8 through a first T-shaped connector 5, and the backflow slurry causes pipe belt fluctuation when flowing in the tank bottom flexible disturbance pipe belt 8, so that the effect of disturbing the slurry and preventing the precipitation is achieved;
thirdly, keeping the flow velocity of the slurry in the pipeline at 2m/s during operation;
when the system is stopped, the washing water pump 4 is started to wash the slurry inside the pipeline to prevent the slurry from depositing in the pipeline;
and when the ambient temperature is higher than 40 ℃, the flushing water pump is periodically started, the slurry in the storage tank 1 is cooled through the cooling nozzle 10, and the loss water of evaporation is replenished.
In the description of the present invention, unless otherwise expressly specified or limited, the terms "mounted," "connected," and "fixed" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral part; can be mechanically or electrically connected; either directly or indirectly through intervening media, either internally or in any other relationship. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
The standard parts used in the invention can be purchased from the market, the special-shaped parts can be customized according to the description of the specification and the accompanying drawings, the specific connection mode of each part adopts conventional means such as bolts, rivets, welding and the like mature in the prior art, the machines, the parts and equipment adopt conventional models in the prior art, and the circuit connection adopts the conventional connection mode in the prior art, so that the detailed description is omitted.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (10)
1. The utility model provides a magnesium hydrate thick liquids feeding device, includes storage tank (1), the lateral wall of storage tank (1) runs through and is equipped with bleeder valve (2), bleeder valve (2) have desulfurizing tower thick liquids pond (3) through pipe connection, be equipped with feed pump (4) on bleeder valve (2), its characterized in that: the desulfurization tower slurry tank is characterized in that one end of a loop pipeline (6) is connected to the guide pipe through a first T-shaped connector (5), the other end of the loop pipeline (6) is connected with the storage tank (1), and a flow regulating valve (7) is arranged on the guide pipe and corresponds to the desulfurization tower slurry tank (3) and is arranged between the first T-shaped connector (5).
2. The magnesium hydroxide slurry supply apparatus according to claim 1, wherein: the loop pipeline (6) is positioned on the side wall of the storage tank (1) and corresponds to the lower end of the discharge valve (2).
3. The magnesium hydroxide slurry supply apparatus according to claim 2, wherein: the lower end of the inner surface of the storage tank (1) is fixedly connected with a flexible disturbance belt (8).
4. The magnesium hydroxide slurry supply apparatus according to claim 1, wherein: still including flushing pipe way (9), be equipped with the washing water pump on flushing pipe way (9), the last lateral wall of storage tank (1) runs through and is equipped with cooling nozzle (10), flushing pipe way (9) with cooling nozzle (10) union coupling.
5. The magnesium hydroxide slurry supply apparatus according to claim 4, wherein: the catheter is provided with a plurality of second T-shaped connectors (11), and the flushing pipeline (9) is respectively connected with the second T-shaped connectors (11) through pipes.
6. The magnesium hydroxide slurry supply apparatus according to claim 3, characterized in that: a plurality of openings are arranged on the flexible disturbance band (8); the openings arranged on the flexible disturbance band are distributed in a downward cross mode.
7. The magnesium hydroxide slurry supply apparatus according to claim 3, characterized in that: the feeding pump (4) is one of a diaphragm pump, a slurry pump or a screw pump.
8. Use of the magnesium hydroxide slurry supply apparatus according to claim 4, comprising the steps of:
firstly, incoming materials enter a storage tank (1) through a feeding hole on the storage tank (1) to be stored for later use;
secondly, when the system operates, a discharge valve (2) and a feed pump (4) are opened, the flow is regulated and controlled by controlling a flow regulating valve (7), redundant slurry flows back to a tank bottom flexible disturbance pipe belt (8) through a first T-shaped connector (5), the pipe belt fluctuation is caused when the backflow slurry flows in the tank bottom flexible disturbance pipe belt (8), and the effect of disturbing the slurry and preventing the precipitation is achieved;
thirdly, keeping the flow velocity of the slurry in the pipeline not higher than 5m/s during operation;
and fourthly, when the magnesium hydroxide slurry supply device is stopped, starting a washing water pump to wash the slurry inside the pipeline to prevent the slurry from depositing in the pipeline.
9. Use of the magnesium hydroxide slurry supply apparatus according to claim 8, wherein: the magnesium hydroxide slurry supply device is also connected with a desulfurizing tower, and the desulfurizing tower is provided with a slurry pool; and the flow regulation and control step is to regulate and control the flow of the magnesium hydroxide slurry supply device flowing into the slurry pool of the desulfurization tower.
10. Use of the magnesium hydroxide slurry supply apparatus according to claim 8, wherein: when the ambient temperature is higher than 40 ℃, the flushing water pump (4) is periodically started, the temperature of the contents in the material storage tank (1) is reduced through the cooling nozzle (10), and the loss water of evaporation is supplemented.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011345735.XA CN112340256A (en) | 2020-11-25 | 2020-11-25 | Magnesium hydroxide slurry supply device and application thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011345735.XA CN112340256A (en) | 2020-11-25 | 2020-11-25 | Magnesium hydroxide slurry supply device and application thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112340256A true CN112340256A (en) | 2021-02-09 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011345735.XA Pending CN112340256A (en) | 2020-11-25 | 2020-11-25 | Magnesium hydroxide slurry supply device and application thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112340256A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114589175A (en) * | 2022-01-31 | 2022-06-07 | 浙江汉信科技有限公司 | Control equipment suitable for slurry processing |
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- 2020-11-25 CN CN202011345735.XA patent/CN112340256A/en active Pending
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| CN1629533A (en) * | 2003-12-16 | 2005-06-22 | 金隆铜业有限公司 | Fluid delivery method for preventing pipe fouling and clogging |
| US20100044323A1 (en) * | 2007-01-02 | 2010-02-25 | Magnus Asplund | Separation media slurry tank |
| CN101173734A (en) * | 2007-11-30 | 2008-05-07 | 卢如年 | Discharge aiding method for pipe-line transportation |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114589175A (en) * | 2022-01-31 | 2022-06-07 | 浙江汉信科技有限公司 | Control equipment suitable for slurry processing |
| CN114589175B (en) * | 2022-01-31 | 2024-05-14 | 浙江汉信科技有限公司 | Control equipment suitable for thick liquids processing |
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