CN207159709U - A kind of slurry, water for paper mould supplies back control system - Google Patents
A kind of slurry, water for paper mould supplies back control system Download PDFInfo
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- CN207159709U CN207159709U CN201721017309.7U CN201721017309U CN207159709U CN 207159709 U CN207159709 U CN 207159709U CN 201721017309 U CN201721017309 U CN 201721017309U CN 207159709 U CN207159709 U CN 207159709U
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- slurry
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Abstract
The utility model provides a kind of slurry, water for paper mould and supplies back control system, the slurry, water supply back control system to include mashing unit, filter element and unit with slurry, mashing unit, filter element and unit with slurry include beater, filter, slurry compounding machine and pipeline respectively, flow controller, temperature controller, pressure controller, fluid level controller, consistency controller and control valve are respectively equipped with beater, filter, slurry compounding machine and pipeline, and controls mashing, filtering and slurry with slurry, water to supply back process by controller control valve door.Paper mould provided by the utility model supplies back control system to make slurry, water in paper pulp moulding technology flow supply back step to realize automation mechanized operation with slurry, water, reduce artificial running cost, reduce risk caused by manual operation, the reliability of technique is improved, while also improves production efficiency.
Description
Technical field
The utility model is related to a kind of slurry, water supply back control system, specifically, be related to a kind of paper mould that is used for
Slurry, water supply back control system.
Background technology
Paper mould is a kind of three-dimensional paper technology.It is moulded using waste paper as raw material on mould machine by certain moduli tool
Go out the paper products of definite shape.Paper mould, in addition to cutlery box, tableware is made, industrial buffering package is more done, development is very fast at present
Speed.The technological process of paper mould include mashing, the slurries removal of impurity, it is with slurry, copy base and deep dehydration, be hot-forming, examine, disappear
Poison and packaging and storage, wherein mashing, the slurries removal of impurity and it is with slurry be by paper stock from it is solid state transformed to liquid make paper pulp raw material
The process of important step, traditional paper pulp moulding technology and family workshop type production technology is all to use manual control, and this is not only
Labor intensive cost, operating process is produced many uncertainties, cause unstable product quality and production efficiency is low etc. asks
Topic.
Utility model content
In place of solving above-mentioned the deficiencies in the prior art, the purpose of this utility model is that providing one kind is used for paper pulp die
Slurry, the water of modeling supply back control system, the defects of to overcome in the prior art.
To achieve these goals, the utility model provides a kind of slurry, water for paper mould and supplies back control system,
The slurry, water supply back control system to include mashing unit, filter element and unit with slurry；Wherein, be beaten unit include beater,
First water inlet pipe, the first regulating valve, heater and the first slurry discharge pipe, beater left upper portion are provided with the first water inlet pipe, the
One water inlet pipe is provided with the first regulating valve, is provided with the first fluid level controller at the top of beater, the first fluid level controller is electrically connected to
First regulating valve and the opening and closing for controlling the first regulating valve, beater left side central portion are provided with the first consistency controller, the first concentration control
Device processed is electrically connected to the first regulating valve and adjusts the opening degree of the first regulating valve, and the left lower of beater is provided with temperature control
Device, temperature controller are electrically connected to the heater of mashing motor spindle, and control the degree of heat of heater, beater bottom right
Provided with the first slurry discharge pipe；Filter element includes filter, the first slurry feed pipe, conveying pump unit, the second water inlet pipe, the
Two regulating valves, the second slurry discharge pipe and the 3rd regulating valve, filter left upper portion are provided with the first slurry feed pipe, the first slurries
Feed pipe is connected with conveying pump unit, and conveying pump unit is connected with the second water inlet pipe and the first slurry discharge pipe, and second enters
Water pipe is provided with the second regulating valve, and the first slurry discharge pipe is provided with the second consistency controller, the electrical connection of the second consistency controller
In the second regulating valve and the opening degree of the second regulating valve is adjusted, filter bottom right side is provided with the second slurry discharge pipe, and second
Slurry discharge pipe is provided with the 3rd regulating valve；Unit with slurry includes slurry compounding machine, the 3rd water inlet pipe, the 4th regulating valve, auxiliary agent charging
Pipe and the 5th regulating valve, motor spindle with slurry connects with the second slurry discharge pipe and the 3rd water inlet pipe, and the 3rd water inlet pipe is provided with the
Four regulating valves, slurry compounding machine top are provided with the second fluid level controller, and the second fluid level controller is electrically connected to the 3rd regulating valve and the 4th
Regulating valve, and the opening and closing of the 3rd regulating valve and the 4th regulating valve is controlled, slurry compounding machine lower right side is provided with the second consistency controller, the
Two consistency controllers are electrically connected to the 3rd regulating valve and the 4th regulating valve, and adjust the opening of the 3rd regulating valve and the 4th regulating valve
Degree, the second fluid level controller right side are provided with auxiliary agent feed pipe, and auxiliary agent feed pipe is provided with flow controller and the 5th regulating valve,
Flow controller is electrically connected to the 5th regulating valve, and controls the opening degree of the 5th regulating valve.
As the further explanation for supplying back slurry described in the utility model, water control system, it is preferable that conveying pump unit
Including delivery pump pipeline, delivery pump branch road, delivery pump, pressure controller and the branch road valve in parallel with delivery pump pipeline, conveying
Pump conduit is connected by delivery pump with the first slurry feed pipe, and delivery pump branch road forms one with delivery pump pipeline connection and followed certainly
Ring path, delivery pump branch road are provided with branch road valve, pressure controller is electrically connected to branch road valve, and controlling brancher valve is opened
Close.
As the further explanation for supplying back slurry described in the utility model, water control system, it is preferable that delivery pump is just
Displacement pump.
The further explanation of control system is supplied back as to slurry described in the utility model, water, it is preferable that branch road valve is
Electric gate valve.
As the further explanation for supplying back slurry described in the utility model, water control system, it is preferable that the first water inlet pipe
On be additionally provided with first flowmeter.
As the further explanation for supplying back slurry described in the utility model, water control system, it is preferable that the second slurries go out
Second flowmeter is additionally provided with expects pipe.
As the further explanation for supplying back slurry described in the utility model, water control system, it is preferable that the 3rd water inlet pipe
On be additionally provided with the 3rd flowmeter.
As the further explanation for supplying back slurry described in the utility model, water control system, it is preferable that the first regulation
Valve, the second regulating valve, the 3rd regulating valve, the 4th regulating valve and the 5th regulating valve are electric control valve.
Paper mould provided by the utility model slurry, water supply back control system make the slurry in paper pulp moulding technology flow,
Water supplies back step to realize automation mechanized operation, reduces artificial running cost, reduces risk caused by manual operation, improves
The reliability of technique, while also improve production efficiency.
Brief description of the drawings
Fig. 1 supplies back the structural representation of control system for the utility model paper mould slurry, water.
Description of reference numerals is as follows：
Unit 1, beater 11, the first fluid level controller 12, the first water inlet pipe 13, first flowmeter 14, first is beaten to adjust
Save valve 15, the first consistency controller 16, temperature controller 17, heater 18, the first slurry discharge pipe 19, filter element 2, filtering
Machine 21, the first slurry feed pipe 22, conveying pump unit 23, delivery pump pipeline 231, delivery pump branch road 232, delivery pump 233, pressure
Controller 234, branch road valve 235, the second water inlet pipe 24, the second regulating valve 25, the second consistency controller 26, the second slurry discharge
Pipe 27, second flowmeter 28, the 3rd regulating valve 29, unit with slurry 3, slurry compounding machine 31, the 3rd water inlet pipe 32, the 3rd flowmeter 33,
4th regulating valve 34, the second consistency controller 35, the second fluid level controller 36, auxiliary agent feed pipe 37, flow controller the 38, the 5th
Regulating valve 39.
Embodiment
In order to further appreciate that structure, feature and other purposes of the present utility model, preferably implement in conjunction with appended
Example be accompanied by accompanying drawing describe in detail it is as follows, this accompanying drawing embodiment described is merely to illustrate the technical solution of the utility model, and
Non-limiting the utility model.
As shown in figure 1, Fig. 1 supplies back the structural representation of control system for the utility model paper mould slurry, water；It is described
Slurry, water supply back control system to include mashing unit 1, filter element 2 and unit with slurry 3；Wherein, mashing unit 1 includes beater
11st, the first water inlet pipe 13, the first regulating valve 15, the slurry discharge pipe 19 of heater 18 and first, the top of beater 11 are provided with first
Fluid level controller 12 is used to monitor and control the liquid level of beater 11, and the left upper portion of beater 11 is provided with the first water inlet pipe 13, the
The regulating valve 15 of first flowmeter 14 and first is sequentially provided with one water inlet pipe 13, the first regulating valve 15 is electrically connected to the first liquid level control
Device 12 processed, and control it to open or close by the first fluid level controller 12.When liquid level reaches the first Liquid level in beater 11
First fluid level controller 12 is alarmed and controls the first regulating valve 15 to close during the preset critical of device 12, is stopped into beater 11
Water is conveyed, prevents that ororrhea goes out in beater 11, first fluid level controller 12 is controlled again when liquid level recovers normal in beater 11
The first regulating valve 15 is made to open.The left side central portion of beater 11 is provided with the first consistency controller 16, and the first consistency controller 16 is electrically connected
It is connected to the first regulating valve 15 and adjusts the opening degree of the first regulating valve 15, the first consistency controller 16 input paper is first given during production
Concentration preset value is starched, when the first consistency controller 16 detects that pulp density and preset value have gap, is adjusted by regulation first
The opening degree of valve 15 is saved so as to control inflow to increase or reduce, so that pulp density is qualified.Under the left side of beater 11
Portion is provided with temperature controller 17, and temperature controller 17 is electrically connected to the heater 18 of the bottom of beater 11, and controls heater 18
Degree of heat, heater 18 be used for give paper pulp heating, prevent paper pulp supercooling viscosity increase be not easy to flow, production before give temperature control
Device 17 processed inputs safe temperature range, just adjusts and adds when temperature controller 17 detects that pulp temperatures exceed preset temperature range
The degree of heat of hot device 18, prevents pulp temperatures too high or too low, and the bottom right of beater 11 is provided with the first slurry discharge pipe
19。
As shown in figure 1, filter element 2 enters including filter 21, the first slurry feed pipe 22, conveying pump unit 23, second
Water pipe 24, the second regulating valve 25, the second slurry discharge pipe 27 and the 3rd regulating valve 29, the left upper portion of filter 21 are provided with the first slurry
Liquid feed pipe 22, the first slurry feed pipe 22 are connected with conveying the export pipeline of pump unit 23, and conveying pump unit 23 includes defeated
Send pump conduit 231, the delivery pump branch road 232 in parallel with delivery pump pipeline 231, delivery pump 233, pressure controller 234 and branch road
Valve 235, delivery pump pipeline 231 are connected by delivery pump 233 with the first slurry feed pipe 22, delivery pump branch road 232 with it is defeated
The connection of pump conduit 231 is sent to form a self-loopa path, delivery pump branch road 232 is provided with branch road valve 235, pressure controller
234 are electrically connected to branch road valve 235, and the opening and closing of controlling brancher valve 235, and delivery pump 233 is positive-dispacement pump, branch road valve
235 be electric gate valve.Because delivery pump 233 uses positive-dispacement pump, the filter process of paper pulp is divided into the constant pressure filtration again of first constant speed, opened
Beginning after filtering, the outlet pressure of delivery pump 233 gradually rises, when outlet pressure reaches the preset pressure value of pressure controller 234,
Can controlling brancher valve 235 automatically turn on, part size return the entrance of delivery pump 233, start constant pressure filtration.Using this filtering
Mode power consumption is few, saves the energy, cost-effective.The second water inlet pipe for conveying the inlet ductwork of pump unit 23 and being mutually in parallel
24 are connected with the first slurry discharge pipe 19, and the second water inlet pipe 24 is provided with the second regulating valve 25, on the first slurry discharge pipe 19
Provided with the second consistency controller 26, the second consistency controller 26 is electrically connected to the second regulating valve 25 and adjusts the second regulating valve 25
Opening degree, when the second consistency controller 26 detects that pulp density exceedes default delivery pump in the first slurry discharge pipe 19
233 when can convey maximum concentration value, and the second consistency controller 26 adjusts the opening degree of the second regulating valve 25, increase water dilution
Paper pulp, prevent from blocking delivery pump 233.The bottom right side of filter 21 is provided with the second slurry discharge pipe 27, the second slurry discharge pipe 27
On be sequentially provided with the regulating valve 29 of second flowmeter 28 and the 3rd.
As shown in figure 1, unit 3 with slurry includes slurry compounding machine 31, the 3rd water inlet pipe 32, the 4th regulating valve 34, auxiliary agent feed pipe
37 and the 5th regulating valve 39, the bottom of slurry compounding machine 31 connected with the second slurry discharge pipe 27 and the 3rd water inlet pipe 32, the 3rd water inlet pipe
The 3rd flowmeter 33 and the 4th regulating valve 34 are sequentially provided with 32, the lower right side of slurry compounding machine 31 is provided with the second consistency controller 35,
Second consistency controller 35 is electrically connected to the 3rd regulating valve 29 and the 4th regulating valve 34, and adjusts the 3rd regulating valve 29 and the 4th and adjust
The opening degree of valve 34 is saved, when pulp density is not up to preset concentration in slurry compounding machine 31, the second consistency controller 35 regulation the
Three regulating valves 29 and the 4th regulating valve 34, so as to adjust the inlet amount of paper pulp and water, so that pulp density is qualified.Slurry compounding machine 31 pushes up
Portion is provided with the second fluid level controller 36, and the second fluid level controller 36 is electrically connected to the 3rd regulating valve 29 and the 4th regulating valve 34, and
The 3rd regulating valve 29 and the 4th regulating valve 34 are adjusted, when liquid level reaches preset critical in slurry compounding machine 31, the second Liquid level
Device 36 is alarmed and controls the 3rd regulating valve 29 and the 4th regulating valve 34 to close, and prevents that ororrhea goes out in slurry compounding machine 31.Second liquid level
The right side of controller 36 is provided with auxiliary agent feed pipe 37, and the regulating valve of flow controller 38 and the 5th is sequentially provided with auxiliary agent feed pipe 37
39, flow controller 38 is electrically connected to the 5th regulating valve 39, and controls the opening degree of the 5th regulating valve 39, flow controller 38
5th regulating valve 39 is controlled according to default auxiliary agent flow value, so as to the auxiliary agent of control input appropriate amount.
It is to be understood that above-mentioned utility model content and embodiment are intended to prove that the utility model provides skill
The practical application of art scheme, it should not be construed as the restriction to scope of protection of the utility model.Those skilled in the art are in this practicality
In new spirit and principle, when can various modifications may be made, equivalent substitution or improvement.The scope of protection of the utility model is with appended power
Sharp claim is defined.
Claims (8)
1. a kind of slurry, water for paper mould supplies back control system, it is characterised in that the slurry, water supply back control system bag
Include mashing unit (1), filter element (2) and unit with slurry (3)；Wherein,
Being beaten unit (1) includes beater (11), the first water inlet pipe (13), the first regulating valve (15), heater (18) and first
Slurry discharge pipe (19), beater (11) left upper portion are provided with the first water inlet pipe (13), and the first water inlet pipe (13) is provided with first
Regulating valve (15), is provided with the first fluid level controller (12) at the top of beater (11), and the first fluid level controller (12) is electrically connected to the
One regulating valve (15) and the opening and closing for controlling the first regulating valve (15), beater (11) left side central portion are provided with the first consistency controller
(16), the first consistency controller (16) is electrically connected to the first regulating valve (15) and adjusts the opening degree of the first regulating valve (15),
The left lower of beater (11) is provided with temperature controller (17), and temperature controller (17) is electrically connected to beater (11) bottom
Heater (18), and the degree of heat of heater (18) is controlled, beater (11) bottom right is provided with the first slurry discharge pipe
(19)；
Filter element (2) includes filter (21), the first slurry feed pipe (22), conveying pump unit (23), the second water inlet pipe
(24), the second regulating valve (25), the second slurry discharge pipe (27) and the 3rd regulating valve (29), filter (21) left upper portion are provided with
First slurry feed pipe (22), the first slurry feed pipe (22) with conveying pump unit (23) be connected, conveying pump unit (23) with
Second water inlet pipe (24) is connected with the first slurry discharge pipe (19), and the second water inlet pipe (24) is provided with the second regulating valve (25),
First slurry discharge pipe (19) is provided with the second consistency controller (26), and the second consistency controller (26) is electrically connected to the second regulation
Valve (25) and the opening degree for adjusting the second regulating valve (25), filter (21) bottom right side are provided with the second slurry discharge pipe
(27), the second slurry discharge pipe (27) is provided with the 3rd regulating valve (29)；
Unit (3) with slurry include slurry compounding machine (31), the 3rd water inlet pipe (32), the 4th regulating valve (34), auxiliary agent feed pipe (37) and
5th regulating valve (39), slurry compounding machine (31) bottom connect with the second slurry discharge pipe (27) and the 3rd water inlet pipe (32), and the 3rd enters
Water pipe (32) is provided with the 4th regulating valve (34), and the second fluid level controller (36), the second liquid level control are provided with the top of slurry compounding machine (31)
Device (36) processed is electrically connected to the 3rd regulating valve (29) and the 4th regulating valve (34), and controls the 3rd regulating valve (29) and the 4th regulation
The opening and closing of valve (34), slurry compounding machine (31) lower right side are provided with the second consistency controller (35), and the second consistency controller (35) is electrically connected
The 3rd regulating valve (29) and the 4th regulating valve (34) are connected to, and adjusts the opening of the 3rd regulating valve (29) and the 4th regulating valve (34)
Degree, the second fluid level controller (36) right side are provided with auxiliary agent feed pipe (37), and auxiliary agent feed pipe (37) is provided with flow controller
(38) and the 5th regulating valve (39), flow controller (38) are electrically connected to the 5th regulating valve (39), and the 5th regulating valve of control
(39) opening degree.
2. slurry as claimed in claim 1, water supply back control system, it is characterised in that conveying pump unit (23) includes delivery pump
Pipeline (231), the delivery pump branch road (232) in parallel with delivery pump pipeline (231), delivery pump (233), pressure controller (234)
With branch road valve (235), delivery pump pipeline (231) is connected by delivery pump (233) with the first slurry feed pipe (22), conveying
Pump branch road (232) connects with delivery pump pipeline (231) forms a self-loopa path, and delivery pump branch road (232) is provided with branch road
Valve (235), pressure controller (234) are electrically connected to branch road valve (235), and the opening and closing of controlling brancher valve (235).
3. slurry as claimed in claim 2, water supply back control system, it is characterised in that delivery pump (233) is positive-dispacement pump.
4. slurry as claimed in claim 2, water supply back control system, it is characterised in that branch road valve (235) is electric gate valve.
5. slurry as claimed in claim 1, water supply back control system, it is characterised in that the is additionally provided with the first water inlet pipe (13)
Flow meters (14).
6. slurry as claimed in claim 1, water supply back control system, it is characterised in that are also set on the second slurry discharge pipe (27)
There is second flowmeter (28).
7. slurry as claimed in claim 1, water supply back control system, it is characterised in that the is additionally provided with the 3rd water inlet pipe (32)
Three flowmeters (33).
8. slurry as claimed in claim 1, water supply back control system, it is characterised in that the first regulating valve (15), the second regulating valve
(25), the 3rd regulating valve (29), the 4th regulating valve (34) and the 5th regulating valve (39) are electric control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721017309.7U CN207159709U (en) | 2017-08-15 | 2017-08-15 | A kind of slurry, water for paper mould supplies back control system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721017309.7U CN207159709U (en) | 2017-08-15 | 2017-08-15 | A kind of slurry, water for paper mould supplies back control system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207159709U true CN207159709U (en) | 2018-03-30 |
Family
ID=61717285
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721017309.7U Active CN207159709U (en) | 2017-08-15 | 2017-08-15 | A kind of slurry, water for paper mould supplies back control system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207159709U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI774609B (en) * | 2021-11-10 | 2022-08-11 | 蕭富林 | Slurry conveying system |
-
2017
- 2017-08-15 CN CN201721017309.7U patent/CN207159709U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI774609B (en) * | 2021-11-10 | 2022-08-11 | 蕭富林 | Slurry conveying system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A pulp and water supply and return control system for pulp molding Effective date of registration: 20220314 Granted publication date: 20180330 Pledgee: Xiamen Huli District Financing Guarantee Co.,Ltd. Pledgor: GEOTEGRITY ECO PACK (XIAMEN) Co.,Ltd. Registration number: Y2022980002564 |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 361100 no.523 Ji'an Road, Tong'an industrial concentration zone, Tong'an District, Xiamen City, Fujian Province Patentee after: Far East Zhongqian (Xiamen) Technology Group Co.,Ltd. Address before: 361100 no.523 Ji'an Road, Tong'an industrial concentration zone, Tong'an District, Xiamen City, Fujian Province Patentee before: GEOTEGRITY ECO PACK (XIAMEN) Co.,Ltd. |