CN114733653B - Seaweed fertilizer stoste two-stage separation equipment - Google Patents
Seaweed fertilizer stoste two-stage separation equipment Download PDFInfo
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- CN114733653B CN114733653B CN202210445859.8A CN202210445859A CN114733653B CN 114733653 B CN114733653 B CN 114733653B CN 202210445859 A CN202210445859 A CN 202210445859A CN 114733653 B CN114733653 B CN 114733653B
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- collecting box
- turbid liquid
- filter belt
- liquid
- centrifuge
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- 241001474374 Blennius Species 0.000 title claims abstract description 35
- 239000003337 fertilizer Substances 0.000 title claims abstract description 33
- 238000000926 separation method Methods 0.000 title claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 149
- 239000000463 material Substances 0.000 claims abstract description 30
- 238000007599 discharging Methods 0.000 claims abstract description 19
- 239000012535 impurity Substances 0.000 claims abstract description 14
- 238000001914 filtration Methods 0.000 claims description 20
- 238000007790 scraping Methods 0.000 claims description 13
- 230000000903 blocking effect Effects 0.000 claims description 8
- 230000007246 mechanism Effects 0.000 claims description 8
- 239000000203 mixture Substances 0.000 abstract description 11
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 11
- 239000011550 stock solution Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 230000009471 action Effects 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 230000000149 penetrating effect Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000199919 Phaeophyceae Species 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002609 medium Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
- B04B5/10—Centrifuges combined with other apparatus, e.g. electrostatic separators; Sets or systems of several centrifuges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
- B01D36/045—Combination of filters with centrifugal separation devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B11/00—Feeding, charging, or discharging bowls
- B04B11/06—Arrangement of distributors or collectors in centrifuges
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Centrifugal Separators (AREA)
Abstract
The invention discloses seaweed fertilizer raw liquid two-stage separation equipment which comprises a turbine centrifuge and a disc centrifuge, wherein a first feeding pipeline is arranged at a feeding port of the turbine centrifuge, a coarse material discharge pipe and a turbid liquid discharge pipe are arranged at the lower side of the turbine centrifuge, a turbid liquid collection box is arranged below the turbid liquid discharge pipe, and a pump body is arranged in the turbid liquid collection box; the feeding port of the disc type centrifugal machine is provided with a second feeding pipeline which extends into the turbid liquid collecting box and is connected with the output end of the pump body, the top of the disc type centrifugal machine is provided with a clear liquid discharging pipe, and the side part of the disc type centrifugal machine is provided with a fine impurity discharging pipe; the seaweed forms the stoste mixture after enzymolysis, carries the first inlet pipe of stoste mixture to the turbo-centrifuge in carry out first separation, and the pump body draws turbid liquid again and carries out the secondary separation in carrying dish-type centrifuge through second feed pipeline, discharges the seaweed fertilizer clear liquid through clear liquid discharge pipe, has improved the clear degree of production seaweed fertilizer stoste, and the quality of seaweed fertilizer stoste is high.
Description
Technical Field
The invention relates to the technical field of seaweed fertilizer production, in particular to seaweed fertilizer raw liquid two-stage separation equipment.
Background
The seaweed fertilizer is a fertilizer which is produced and processed by using marine brown algae or is processed by adding a certain amount of nitrogen, phosphorus, potassium and medium trace elements. There are various forms, mainly liquid and powder are used in the market, and a small part of the liquid and powder are in a granular state, so that marine brown algae contains various substances.
The seaweed fertilizer needs to separate solid materials in the seaweed fertilizer stock solution in the growing process, the prior art has poor effect in separation, the seaweed fertilizer stock solution contains fine plant tissues, the seaweed fertilizer stock solution is turbid, and the production quality does not meet the requirements.
Disclosure of Invention
The invention aims to provide a seaweed fertilizer raw liquid two-stage separation device, which aims to solve the problems in the background technology.
In order to achieve the above purpose, the present invention provides the following technical solutions: the seaweed fertilizer raw liquid two-stage separation device comprises a turbine centrifuge and a disc centrifuge, wherein a first feeding pipeline is arranged at a feed inlet of the turbine centrifuge, a coarse material discharge pipe and a turbid liquid discharge pipe are arranged at the lower side of the turbine centrifuge, a turbid liquid collection box is arranged below the turbid liquid discharge pipe, and a pump body is arranged in the turbid liquid collection box;
The disc centrifuge feeding port is provided with a second feeding pipeline, the second feeding pipeline extends into the turbid liquid collecting box and is connected with the output end of the pump body, the top of the disc centrifuge is provided with a clear liquid discharging pipe, and the side part of the disc centrifuge is provided with a fine impurity discharging pipe.
As a preferable technical scheme of the invention, a coarse material collecting box is arranged below the coarse material discharging pipe.
As a preferable technical scheme of the invention, a fine material collecting box is arranged below the fine impurity discharging pipe.
As a preferable technical scheme of the invention, a filtering mechanism is arranged above a pump body in the turbid liquid collecting box, the filtering mechanism comprises two groups of rotating rollers rotatably arranged on the inner wall of the turbid liquid collecting box, the two groups of rotating rollers are arranged in a left-low-right-high mode, filtering belts are sleeved on the two groups of rotating rollers, a turbid liquid discharging pipe vertically extends downwards to the middle part of the upper side of the filtering belts, a driving source is arranged on the outer wall of the turbid liquid collecting box, and the driving source is in driving connection with one group of rotating rollers through a belt pulley group to drive the filtering belts to rotate anticlockwise.
As a preferable technical scheme of the invention, the liquid blocking plates are fixedly connected to the two sides of the filter belt.
As a preferable technical scheme of the invention, the turbid liquid collecting box is provided with a first collecting box on the outer wall of the right side, a first scraping plate is arranged in the first collecting box, the first scraping plate extends obliquely upwards and contacts with the filter belt to scrape plant tissues on the upper side of the filter belt, and a first liquid draining hole communicated with the turbid liquid collecting box is formed in the bottom wall of the first collecting box.
As a preferable technical scheme of the invention, the turbid liquid collecting box is provided with a second collecting box on the outer wall of the left side, a second scraping plate is arranged in the second collecting box, the second scraping plate extends obliquely upwards and contacts with the filter belt to scrape plant tissues at the lower side of the filter belt, and a second liquid draining hole communicated with the turbid liquid collecting box is formed in the bottom wall of the second collecting box.
As a preferable technical scheme of the invention, the side walls of the first collecting box and the second collecting box are respectively provided with an electric control push rod, and the movable end of the electric control push rod is connected with a push plate.
Compared with the prior art, the invention has the beneficial effects that: according to the seaweed fertilizer raw liquid two-stage separation equipment, seaweed is subjected to enzymolysis to form a raw liquid mixture, a first feed pipe of the raw liquid mixture is conveyed into a turbine centrifuge for first separation, coarse plant impurities in the raw liquid mixture are discharged through a coarse material discharge pipe, the primarily separated turbid liquid is discharged into a turbid liquid collecting box through a turbid liquid discharge pipe, a pump body extracts the turbid liquid again and conveys the turbid liquid into a disc centrifuge through a second feed pipeline for second separation, fine plant impurities are discharged through a fine impurity discharge pipe, seaweed fertilizer clear liquid is discharged through a clear liquid discharge pipe, the clarity of the seaweed fertilizer raw liquid produced is improved, and the quality of the seaweed fertilizer raw liquid is high;
The turbid liquid discharged by the turbid liquid discharge pipe is firstly dropped to the middle part of the upper side of the filter belt, the turbid liquid moves downwards along the filter belt under the action of self gravity, the driving source drives a group of rotating rollers to rotate through the belt pulley group and drives the filter belt to rotate anticlockwise, so that the filter belt is fully contacted with the turbid liquid, thicker plant tissues remained in the downward movement process of the turbid liquid can be left on the filter belt, the turbid liquid falls into the turbid liquid collecting box through the filtering holes penetrating through the filter belt, the effect of intermediate filtration on the seaweed fertilizer turbid liquid is realized, the separation effect on a stock solution mixture is further improved after the subsequent separation by the disc type centrifugal machine, the quality of the seaweed fertilizer stock solution is high, the turbid liquid can not fall along the gap between the filter belt and the turbid liquid collecting box by the liquid blocking plate, the blocking effect on the turbid liquid is realized, and the filtering effect is good;
When the filter belt rotates anticlockwise to continuously filter turbid liquid in the middle, the turbid liquid sequentially passes through the upper layer of the filter belt and the lower layer of the filter belt to be filtered for two times, plant tissues at the upper side of the filter belt are scraped into the first collecting box through the first scraping plate, plant tissues at the lower side of the filter belt are scraped into the first collecting box through the second scraping plate, so that the plant tissues can not continuously exist in the outer side of the filter belt in the continuous movement process, the filtering effect of the filter belt on the turbid liquid is ensured, the turbid liquid carried in the plant tissues of the first collecting box and the second collecting box can enter the turbid liquid collecting box through the first liquid discharge hole and the second liquid discharge hole, meanwhile, the electric control push rod can be controlled to drive the push plate to stretch out at regular time, the plant tissues in the first collecting box and the second collecting box are extruded, the turbid liquid carried by the electric control push rod is effectively discharged into the turbid liquid collecting box, the utilization rate of the turbid liquid is high, and the plant tissues after the extrusion is convenient for workers to take out the plant tissues;
the coarse material collecting box collects the plant coarse material discharged by the turbine centrifugal machine, and the fine material collecting box collects the plant fine material discharged by the disc centrifugal machine, so that the plant coarse material and the plant fine material can be collected and reused, and the resource utilization rate is high.
Drawings
FIG. 1 is a schematic diagram of the overall structure of the present invention;
FIG. 2 is a schematic view of the structure of the turbo-centrifuge of the present invention;
FIG. 3 is a schematic diagram of the internal structure of the turbid liquid collecting box of the invention;
FIG. 4 is a schematic view of a disk centrifuge according to the present invention;
in the figure: 100. a turbo centrifuge; 110. a first feed conduit; 120. a turbid liquid discharge pipe; 121. a turbid liquid collecting box; 130. a coarse material discharge pipe; 131. a coarse material collecting box; 140. a filtering mechanism; 141. a rotating roller; 142. a filter belt; 143. a liquid blocking plate; 144. a first collection box; 1441. a first scraper; 1442. a first drain hole; 145. a second collection box; 1451. a second scraper; 1452. a second drain hole; 150. a driving source; 151. a belt pulley set; 160. an electric control push rod; 161. a push plate; 200. a disk centrifuge; 210. a second feed conduit; 211. a pump body; 220. a clear liquid discharge pipe; 230. a fine impurity discharging pipe; 231. and a fine material collecting box.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
In the description of the present invention, it should be noted that the azimuth or positional relationship indicated by the terms "vertical", "upper", "lower", "horizontal", etc. are based on the azimuth or positional relationship shown in the drawings, and are merely for convenience of describing the present invention and simplifying the description, and do not indicate or imply that the apparatus or element referred to must have a specific azimuth, be constructed and operated in a specific azimuth, and thus should not be construed as limiting the present invention.
In the description of the present invention, it should also be noted that, unless explicitly specified and limited otherwise, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present invention can be understood by those of ordinary skill in the art according to the specific circumstances.
Please refer to fig. 1-4
Example 1
The invention provides a technical scheme that: the seaweed fertilizer raw liquid two-stage separation device comprises a turbine centrifuge 100 and a disc centrifuge 200, wherein a first feeding pipeline 110 is arranged at a feed inlet of the turbine centrifuge 100, a coarse material discharge pipe 130 and a turbid liquid discharge pipe 120 are arranged at the lower side of the turbine centrifuge 100, a turbid liquid collecting box 121 is arranged below the turbid liquid discharge pipe 120, and a pump body 211 is arranged in the turbid liquid collecting box 121; the feeding port of the disc centrifuge 200 is provided with a second feeding pipe 210, the second feeding pipe 210 extends into the turbid liquid collecting tank 121 and is connected with the output end of the pump body 211, the top of the disc centrifuge 200 is provided with a clear liquid discharging pipe 220, and the side part is provided with a fine impurity discharging pipe 230.
Specifically, the seaweed forms the stoste mixture after enzymolysis, the first inlet pipe of the stoste mixture is conveyed into the turbine centrifuge 100 for first separation, coarse plant impurities in the stoste mixture are discharged through the coarse material discharge pipe 130, the primarily separated turbid liquid is discharged into the turbid liquid collecting box 121 through the turbid liquid discharge pipe 120, the turbid liquid is pumped by the pump body 211 and conveyed into the disc centrifuge 200 through the second inlet pipe 210 for second separation, fine plant impurities are discharged through the fine impurity discharge pipe 230, the seaweed fertilizer clear liquid is discharged through the clear liquid discharge pipe 220, the clarity of the seaweed fertilizer stoste produced is improved, and the quality of the seaweed fertilizer stoste is high.
Example 2
On the basis of embodiment 1, a filtering mechanism 140 is arranged above a pump body 211 in a turbid liquid collecting box 121, the filtering mechanism 140 comprises two sets of rotating rollers 141 rotatably arranged on the inner wall of the turbid liquid collecting box 121, the two sets of rotating rollers 141 are arranged in a left-low-right-high mode, a filter belt 142 is sleeved on the two sets of rotating rollers 141, a turbid liquid discharging pipe 120 vertically extends downwards to the middle of the upper side of the filter belt 142, a driving source 150 is arranged on the outer wall of the turbid liquid collecting box 121, the driving source 150 is a servo motor, and the driving source 150 is in driving connection with the set of rotating rollers 141 through a belt pulley group 151 to drive the filter belt 142 to rotate anticlockwise.
Specifically, the turbid liquid discharged by the turbid liquid discharge pipe 120 after preliminary separation falls to the middle part of the upper side of the filter belt 142, the turbid liquid moves downwards along the filter belt 142 under the action of self gravity, the driving source 150 drives a group of rotating rollers 141 to rotate through the belt pulley group 151 and drives the filter belt 142 to rotate anticlockwise, the filter belt 142 is enabled to be fully contacted with the turbid liquid, the residual coarser plant tissues of the turbid liquid in the downward movement process can be remained on the filter belt 142, the turbid liquid falls downwards into the turbid liquid collecting box 121 through the filter holes penetrating through the filter belt 142, the effect of intermediate filtration on the seaweed fertilizer turbid liquid is achieved, the separation effect on the stock solution mixture is further improved after the subsequent separation through the disc type centrifugal machine 200, and the quality of the seaweed fertilizer stock solution is high.
Example 3
On the basis of embodiment 1, a filtering mechanism 140 is arranged above a pump body 211 in a turbid liquid collecting box 121, the filtering mechanism 140 comprises two sets of rotating rollers 141 rotatably arranged on the inner wall of the turbid liquid collecting box 121, the two sets of rotating rollers 141 are arranged in a left-low-right-high mode, a filter belt 142 is sleeved on the two sets of rotating rollers 141, a turbid liquid discharging pipe 120 vertically extends downwards to the middle of the upper side of the filter belt 142, a driving source 150 is arranged on the outer wall of the turbid liquid collecting box 121, the driving source 150 is a servo motor, and the driving source 150 is in driving connection with the set of rotating rollers 141 through a belt pulley group 151 to drive the filter belt 142 to rotate anticlockwise, and liquid blocking plates 143 are fixedly connected to two sides of the filter belt 142.
Specifically, the turbid liquid discharged by the turbid liquid discharge pipe 120 falls to the middle part of the upper side of the filter belt 142 firstly, the turbid liquid moves downwards along the filter belt 142 under the action of self gravity, the driving source 150 drives a group of rotating rollers 141 to rotate through the belt pulley group 151 and drives the filter belt 142 to rotate anticlockwise, the filter belt 142 is enabled to be fully contacted with the turbid liquid, the residual thicker plant tissues of the turbid liquid in the downward movement process can be remained on the filter belt 142, the turbid liquid falls downwards into the turbid liquid collecting box 121 through the filter holes penetrating through the filter belt 142, the effect of middle filtration on the seaweed fertilizer turbid liquid is achieved, the separation effect on the stock solution mixture is further improved after the follow-up separation by the disc centrifuge 200, the quality of the seaweed fertilizer stock solution is high, the liquid blocking plate 143 enables the turbid liquid not to fall down along the gap between the filter belt 142 and the turbid liquid collecting box 121, the blocking effect on the turbid liquid is achieved, and the filtering effect is good.
Example 4
On the basis of embodiment 2 or 3, the turbid liquid collecting tank 121 is provided with a first collecting tank 144 on the outer wall on the right side, a first scraping plate 1441 is arranged in the first collecting tank 144, the first scraping plate 1441 extends obliquely upwards and contacts with the filter belt 142 to scrape plant tissues on the upper side of the filter belt 142, and a first liquid discharging hole 1442 communicated with the turbid liquid collecting tank 121 is arranged on the bottom wall of the first collecting tank 144; the turbid liquid collecting box 121 is provided with a second collecting box 145 on the left outer wall, a second scraper 1451 is arranged in the second collecting box 145, the second scraper 1451 extends obliquely upwards and contacts with the filter belt 142 to scrape plant tissues at the lower side of the filter belt 142, and a second liquid discharge hole 1452 communicated with the turbid liquid collecting box 121 is formed in the bottom wall of the second collecting box 145; the side walls of the first collecting box 144 and the second collecting box 145 are respectively provided with an electric control push rod 160, and the movable end of the electric control push rod 160 is connected with a push plate 161.
Specifically, when the filter belt 142 rotates anticlockwise to continuously filter the turbid liquid in the middle, the turbid liquid sequentially passes through the upper layer of the filter belt 142 and the lower layer of the filter belt 142 to be filtered twice, plant tissues at the upper side of the filter belt 142 are scraped into the first collecting box 144 by the first scraping plate 1441, plant tissues at the lower side of the filter belt 142 are scraped into the first collecting box 144 by the second scraping plate 1451, the plant tissues can not continuously exist in the outer side of the filter belt 142 in the continuous movement process, the filtering effect of the filter belt 142 on the turbid liquid is ensured, the turbid liquid carried in the plant tissues of the first collecting box 144 and the second collecting box 145 can enter the turbid liquid collecting box 121 through the first liquid drain hole 1442 and the second drain hole 1452, meanwhile, the electric control push plate 161 can be driven to stretch out by the electric control push plate 161, the plant tissues in the first collecting box 144 and the second collecting box 145 are extruded, the turbid liquid carried by the plant tissues are effectively discharged into the turbid liquid collecting box 121, the utilization rate of the turbid liquid is high, and the plant tissues can be conveniently taken out by workers after the plant tissues are extruded.
Example 5
On the basis of any one of embodiments 1 to 5, a coarse material collecting tank 131 is provided below the coarse material discharging pipe 130; a fine material collecting tank 231 is provided below the fine impurity discharging pipe 230.
Specifically, the coarse material collecting box 131 collects the coarse plant material discharged from the turbo centrifuge 100, and the fine material collecting box 231 collects the fine plant material discharged from the disk centrifuge 200, so that the coarse plant material and the fine plant material can be collected and reused, and the resource utilization rate is high.
Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (3)
1. The seaweed fertilizer raw liquid two-stage separation device is characterized by comprising a turbine centrifuge and a disc centrifuge, wherein a first feeding pipeline is arranged at a feeding port of the turbine centrifuge, a coarse material discharge pipe and a turbid liquid discharge pipe are arranged at the lower side of the turbine centrifuge, a turbid liquid collection box is arranged below the turbid liquid discharge pipe, and a pump body is arranged in the turbid liquid collection box;
the feeding port of the disc type centrifugal machine is provided with a second feeding pipeline which extends into the turbid liquid collecting box and is connected with the output end of the pump body, the top of the disc type centrifugal machine is provided with a clear liquid discharging pipe, and the side part of the disc type centrifugal machine is provided with a fine impurity discharging pipe;
The filtering mechanism is arranged above the pump body in the turbid liquid collecting box and comprises two groups of rotating rollers rotatably arranged on the inner wall of the turbid liquid collecting box, the two groups of rotating rollers are arranged in a left-low and right-high mode, filtering belts are sleeved on the two groups of rotating rollers, the turbid liquid discharge pipe vertically extends downwards to the middle part of the upper side of the filter belt, a driving source is arranged on the outer wall of the turbid liquid collection box, and the driving source is in driving connection with a group of rotating rollers through a belt pulley group to drive the filter belt to rotate anticlockwise; the liquid blocking plates are fixedly connected to the two sides of the filter belt;
The turbid liquid collecting box is characterized in that a first collecting box is arranged on the outer wall of the right side, a first scraping plate is arranged in the first collecting box, extends obliquely upwards and contacts with the filter belt, plant tissues on the upper side of the filter belt are scraped, and a first liquid discharge hole communicated with the turbid liquid collecting box is formed in the bottom wall of the first collecting box;
The turbid liquid collecting box is provided with a second collecting box on the outer wall of the left side, a second scraping plate is arranged in the second collecting box, the second scraping plate extends obliquely upwards and contacts with the filter belt to scrape plant tissues at the lower side of the filter belt, and a second liquid discharge hole communicated with the turbid liquid collecting box is formed in the bottom wall of the second collecting box;
the side walls of the first collecting box and the second collecting box are respectively provided with an electric control push rod, and the movable ends of the electric control push rods are connected with push plates.
2. The seaweed fertilizer raw liquid two-stage separation device of claim 1, wherein a coarse material collecting box is arranged below the coarse material discharging pipe.
3. The seaweed fertilizer raw liquid two-stage separation device of claim 1, wherein a fine material collecting box is arranged below the fine impurity discharging pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210445859.8A CN114733653B (en) | 2022-04-26 | 2022-04-26 | Seaweed fertilizer stoste two-stage separation equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210445859.8A CN114733653B (en) | 2022-04-26 | 2022-04-26 | Seaweed fertilizer stoste two-stage separation equipment |
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| Publication Number | Publication Date |
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| CN114733653A CN114733653A (en) | 2022-07-12 |
| CN114733653B true CN114733653B (en) | 2024-04-16 |
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| CN202210445859.8A Active CN114733653B (en) | 2022-04-26 | 2022-04-26 | Seaweed fertilizer stoste two-stage separation equipment |
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| CN115770412B (en) * | 2023-02-10 | 2023-04-11 | 山东邦迪化学制品股份有限公司 | Production equipment and production process of tetramethyl divinyl disiloxane |
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| CN203155395U (en) * | 2013-04-17 | 2013-08-28 | 青岛中人智业生物科技有限公司 | Tubular/disk-shaped serial centrifugal unit for separating capsaicin in pigment production |
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