CN206139130U - Mixed additive of solid -liquid preparation system - Google Patents
Mixed additive of solid -liquid preparation system Download PDFInfo
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- CN206139130U CN206139130U CN201621099891.1U CN201621099891U CN206139130U CN 206139130 U CN206139130 U CN 206139130U CN 201621099891 U CN201621099891 U CN 201621099891U CN 206139130 U CN206139130 U CN 206139130U
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- mixing channel
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- additive
- preparation system
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Abstract
The utility model discloses a mixed additive of solid -liquid preparation system, technical scheme include the mixing tank, the import of mixing tank is connected with liquid charge -in system and powder charge -in system respectively, the export of mixing tank connects gradually filter, additive pump and product storage tank, the import of mixing tank still is connected with the dust -exhaust of collecting system dust. The utility model discloses the additive performance is effectively guaranteed to degree of automation height, labour saving and time saving, friendly to environment, energy saving and consumption reduction, measurement accuracy.
Description
Technical field
The utility model is related to a kind of additive of chemical field and is mixed with system, specifically a kind of solid-liquid mixing
Additive preparation system.
Background technology
In order that water-coal-slurry has high solids content, low viscosity, good fluidity and stability, in water-coal-slurry preparation process
It is general to add a small amount of additive with dispersion and stabilization.This kind of additive is often complex additive, in preparation process
In need that multiple components are mixed in solution (or water), then reuse, the past generally using mixing after manually weighing respectively, no
Only waste time and energy, user can not be continuously supplied in a large number.In addition, solid material mostly is pulvis, easily produce in mixed process
Fecula dirt, not only pollutes environment, harmful to human, can also cause wastage of material.In mixed process, it is also possible to exist a small amount of insoluble
Thing, it can have a strong impact on the stable operation of the performance of water-coal-slurry and follow-up system in water-coal-slurry.
The content of the invention
The purpose of this utility model is to solve above-mentioned technical problem, there is provided a kind of high degree of automation, it is time saving and energy saving,
Environmentally friendly, energy-saving, accurate measurement, is effectively ensured the solid-liquid additive package preparation system of Additive Properties.
Technical scheme includes mixing channel, and the import of the mixing channel connects respectively with liquid feed line and powder feed system
Connect, the outlet of the mixing channel is sequentially connected filter, additive pump and product storage tank, the import of the mixing channel also with collection
The outlet connection of the deduster of system dust.
The liquid feed line includes tank, water pump and the flowmeter being sequentially connected, and the flowmeter mixes with described
The import connection of groove.
The powder feed system includes ton bag batcher, and the outlet of the ton bag batcher connects multiple feed bins, each
The corresponding Weighing feeders of feed bin Jing are connected with the import of mixing channel.
Beneficial effect：
1. liquid feedstock and powder charging has respective feed system, is capable of achieving automatic feed and metering, effectively replaces
Manually, time saving and energy saving, reduced investment, production capacity is big, efficiency high；
2. the outlet of deduster is connected with mixing channel import, the system dust collected in deduster is sent in mixing channel and returned
With environmental friendliness；
3. filter is set up after mixing channel for filter mix after insoluble matter in material, it is to avoid insoluble matter enters downstream
Product and system；
4. material is sent into into product storage tank, the continuous long-period stable operation of feasible system with additive pump, it is adaptable to big
Type gasifies or fuel coal water slurry production field.
Description of the drawings
Fig. 1 is the utility model schematic diagram.
Wherein：1- ton bag batchers, 2- feed bins, 3- Weighing feeders, 4- feed bins, 5- Weighing feeders, 6- feed bins, 7- claim
Weight batcher, 8- tanks, 9- water pumps, 10- flowmeters, 11- dedusters, 12- mixing channels, 13- filters, 14- additive pumps,
15- product storage tanks, 16- conveying measuring pumps.
Specific embodiment
Below in conjunction with the accompanying drawings explanation is further explained to the utility model：
The discharging opening of ton bag batcher 1 can freely connect feed bin 2, feed bin 4 and feed bin 6, and the discharging opening Jing of feed bin 2 claims
Weight batcher 3 connects the import of mixing channel 12；The weighed batcher 5 of discharging opening of feed bin 4 connects mixing channel 12；The discharging opening of feed bin 6
Weighed batcher 7 connects mixing channel 12；The discharging opening Jing water pumps 9, flowmeter 10 of tank 8 connect the import of mixing channel 12；It is described mixed
Conjunction groove 12 is connected to the deduster 11 of collection system dust and exports.The mixing channel 12 is exported through filter 13, additive pump
14 connect product storage tank 15.When needing to dispense user, the outlet of product storage tank 15 is exported by conveying measuring pump 16 to user.
Technological process：
By three components (A hosts, B hosts, conditioning agent) and as a example by water is prepared according to a certain percentage.A hosts by ton wrap to
Material machine 1 sends into feed bin 2, and mixing channel 12 is added after the metered flow of weighed batcher 3；B hosts send into feed bin by ton bag batcher 1
4, mixing channel 12 is added after the metered flow of weighed batcher 5；Conditioning agent sends into feed bin 6, weighed feed by ton bag batcher 1
Mixing channel 12 is added after the metered flow of machine 7；Water in tank 8 adds mixing channel 12 Jing after water pump 9, the metered flow of flowmeter 10；
Again loopback enters mixing channel 12 after the dust of generation is collected by deduster 11 during the charging of whole system.A hosts, B hosts, tune
Section agent, water and come Self-duster 11 a small amount of dust it is agitated in mixing channel 12 after be sufficiently mixed, then filter through filter 13
Insoluble matter in material, then added dose of pump 14 be delivered to product storage tank 15.Additive product in product storage tank 15 is by defeated
Measuring pump 16 is sent to deliver to user.
Claims (3)
1. a kind of solid-liquid additive package preparation system, including mixing channel, it is characterised in that the import of the mixing channel respectively with
Liquid feed line and powder feed system connect, and the outlet of the mixing channel is sequentially connected filter, additive pump and product
Storage tank, the import of the mixing channel is also connected with the house outlet of collection system dust.
2. solid-liquid additive package preparation system as claimed in claim 1, it is characterised in that the liquid feed line includes
Tank, water pump and the flowmeter being sequentially connected, the flowmeter is connected with the import of the mixing channel.
3. solid-liquid additive package preparation system as claimed in claim 1 or 2, it is characterised in that the powder feed well bag
Include a ton bag batcher, the outlet of the ton bag batcher connects multiple feed bins, the corresponding Weighing feeders of each feed bin Jing with it is mixed
Close the import connection of groove.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621099891.1U CN206139130U (en) | 2016-09-30 | 2016-09-30 | Mixed additive of solid -liquid preparation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621099891.1U CN206139130U (en) | 2016-09-30 | 2016-09-30 | Mixed additive of solid -liquid preparation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206139130U true CN206139130U (en) | 2017-05-03 |
Family
ID=58621275
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621099891.1U Active CN206139130U (en) | 2016-09-30 | 2016-09-30 | Mixed additive of solid -liquid preparation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206139130U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108395983A (en) * | 2018-01-12 | 2018-08-14 | 山东科技大学 | A kind of configuration of culture medium and mineral obtain system |
-
2016
- 2016-09-30 CN CN201621099891.1U patent/CN206139130U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108395983A (en) * | 2018-01-12 | 2018-08-14 | 山东科技大学 | A kind of configuration of culture medium and mineral obtain system |
| CN108395983B (en) * | 2018-01-12 | 2021-09-14 | 山东科技大学 | Culture medium configuration and mineral acquisition system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220530 Address after: No. 1019 Minzu Avenue, Donghu New Technology Development Zone, Wuhan, Hubei 430223 Patentee after: Wuhan Tianyuan Engineering Co.,Ltd. Address before: No. 1019 Minzu Avenue, Donghu New Technology Development Zone, Wuhan, Hubei 430223 Patentee before: Wuhuan Engineering Co.,Ltd. |
|
| TR01 | Transfer of patent right |