CN219930476U - Slurry preparation system - Google Patents

Slurry preparation system Download PDF

Info

Publication number
CN219930476U
CN219930476U CN202320849744.5U CN202320849744U CN219930476U CN 219930476 U CN219930476 U CN 219930476U CN 202320849744 U CN202320849744 U CN 202320849744U CN 219930476 U CN219930476 U CN 219930476U
Authority
CN
China
Prior art keywords
slurry
tank body
liquid outlet
tank
communicated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202320849744.5U
Other languages
Chinese (zh)
Inventor
杨国明
姚慧
张瑜
马哲
鲁学礼
程汇涛
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jushi Group Co Ltd
Original Assignee
Jushi Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jushi Group Co Ltd filed Critical Jushi Group Co Ltd
Priority to CN202320849744.5U priority Critical patent/CN219930476U/en
Application granted granted Critical
Publication of CN219930476U publication Critical patent/CN219930476U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Paper (AREA)

Abstract

The utility model provides a slurry preparation system, comprising: the first slurry part, the second slurry part, the third slurry part and the slurry tank. The first slurry part comprises a feed inlet and is communicated with the water inlet pipeline to prepare slurry; the second slurry part stores the slurry prepared by the first slurry part; the third slurry part is respectively communicated with the second slurry part and the slurry tank; the slurry tank provides slurry for coating the warp of the glass fiber electronic cloth. In the slurry preparation system of the present utility model, a large amount of slurry is prepared in the first slurry section, stored in each of the second slurry sections, and distributed to each of the third slurry sections. The primary batching can be supplied to a plurality of machines for use, so that the batching times are reduced; the first slurry part is discharged into the second slurry part in time after the first slurry part is mixed, the subsequent mixing operation is not influenced, the second slurry part supplements the slurry to the third slurry part in time, and the working efficiency is effectively improved. Meanwhile, the slurry preparation system can accurately control the water supplementing amount and the steam supply amount, and improves the quality stability of the slurry.

Description

Slurry preparation system
Technical Field
The utility model relates to the technical field of slurry preparation equipment, in particular to a slurry preparation system.
Background
The glass fiber electronic cloth is widely applied to the fields of automobiles, communication, aerospace, household appliances, mobile phones and the like, and warp yarns can rub with a dropper, a reed and the like at a high speed in the weaving process of the glass fiber electronic cloth, so that defects such as warp fuzzing and the like are easy to occur, and the product quality is influenced. Therefore, a sizing machine is often adopted for sizing, and special sizing agent is coated on the warp so as to protect the yarns, improve the wear resistance of the yarns and reduce the generation of cloth defects.
The existing slurry preparation tank can only complete slurry preparation, has a single equipment structure, has lower control precision on water supplementing quantity, temperature and the like, and often causes fluctuation of solid content and cooking temperature of the slurry, thereby causing unstable quality of the slurry. Meanwhile, as the productivity of a slurry preparation workshop is enlarged, the number of slurry preparation machines is increased, and the structure of products is diversified, so that a slurry conveying line is longer and longer, the existing slurry preparation equipment is low in production efficiency, high in preparation cost and inconvenient to produce on a large scale.
Disclosure of Invention
To solve the above problems, a slurry preparation system is proposed.
The present utility model provides a slurry formulation system comprising: the first slurry part, the second slurry part, the third slurry part and the slurry tank;
the first slurry part comprises a feed inlet, and is communicated with a water inlet pipeline to prepare slurry; the second slurry part is communicated with the first slurry part so as to store the slurry prepared by the first slurry part;
the third slurry part is communicated with the second slurry part;
the slurry tank is communicated with the third slurry part to provide slurry for coating the warp of the glass fiber electronic cloth;
the ratio of the number of the first slurry part to the number of the second slurry part is 1: n, the ratio of the number of the second slurry portions to the number of the third slurry portions is 1: m, wherein N and M are positive integers greater than or equal to 1.
The third slurry parts are in one-to-one correspondence with the number of the slurry tanks, and the third slurry parts are arranged above the slurry tanks.
Wherein the first slurry portion includes: the device comprises a first tank body, a first stirring mechanism and a first heating mechanism; the feed inlet is arranged on the first tank body; the first tank body further comprises a first liquid inlet and a first liquid outlet;
the first stirring mechanism comprises a first stirrer, and the first stirrer is arranged in the first tank body;
the first heating mechanism comprises a first heating coil and a first heater, the first heating coil is arranged on the inner wall of the first tank body, and the first heater is electrically connected with the first heating coil.
Wherein the second slurry portion includes: the second tank body, the second stirring mechanism and the second heating mechanism; the second tank body further comprises a second liquid inlet and a second liquid outlet; the second liquid outlet is communicated with the first liquid outlet;
the second stirring mechanism comprises a second stirrer, and the second stirrer is arranged in the second tank body;
the second heating mechanism comprises a second heating coil pipe and a second heater, the second heating coil pipe is arranged on the inner wall of the second tank body, and the second heater is electrically connected with the second heating coil pipe;
the third slurry includes: a third tank, a third stirring mechanism and a third heating mechanism; the third tank body further comprises a third liquid inlet and a third liquid outlet; the third liquid outlet is communicated with the second liquid outlet;
the third stirring mechanism comprises a third stirrer, and the third stirrer is arranged in the third tank body;
the third heating mechanism comprises a third heating coil and a third heater, the third heating coil is arranged on the inner wall of the third tank body, and the third heater is electrically connected with the third heating coil.
Wherein the first slurry portion, the second slurry portion, and the third slurry portion further include:
the weighing mechanism is respectively arranged at the bottoms of the first tank body, the second tank body and/or the third tank body.
Wherein the first slurry portion, the second slurry portion, and the third slurry portion further include:
the liquid level meter is arranged on the side wall of the first tank body, the second tank body and/or the third tank body.
And the first liquid outlet, the second liquid outlet and the third liquid outlet are respectively provided with a material level switch.
Wherein the first slurry portion, the second slurry portion, and the third slurry portion further include:
the heat preservation layer is arranged on the inner walls of the first tank body, the second tank body and/or the third tank body respectively.
Wherein, the slurry preparation system also comprises a feeding pipeline and a steam pipeline;
the feeding pipeline and the steam pipeline are respectively communicated with the feeding port;
the steam pipeline is respectively communicated with the first liquid inlet, the second liquid inlet and the third liquid inlet.
The slurry preparation system further comprises a waste liquid pipeline, and the waste liquid pipeline is respectively communicated with the first liquid outlet, the second liquid outlet and the third liquid outlet.
Compared with the prior art, the utility model has the following beneficial effects: in the slurry preparation system of the present utility model, a large amount of slurry is prepared in the first slurry section, stored in each of the second slurry sections, and distributed to each of the third slurry sections. The primary batching can be supplied to a plurality of machines for use, so that the batching times are reduced; the first slurry part is discharged into the second slurry part in time after the first slurry part is mixed, the subsequent mixing operation is not influenced, the second slurry part supplements the slurry to the third slurry part in time, and the working efficiency is effectively improved. Meanwhile, the slurry preparation system can accurately control the water supplementing amount and the steam supply amount, and improves the quality stability of the slurry.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present utility model, the drawings that are needed in the embodiments will be briefly described below, it being understood that the following drawings only illustrate some embodiments of the present utility model and therefore should not be considered as limiting the scope, and other related drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic diagram of a slurry formulation system, according to an exemplary embodiment.
Fig. 2 is a schematic view of a part of the structure of the first slurry section shown in the embodiment.
Fig. 3 is a schematic view of the rest of the structure of the first slurry section shown in the embodiment.
Detailed Description
For the purpose of making the objects, technical solutions and advantages of the embodiments of the present utility model more apparent, the technical solutions of the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model, and it is apparent that the described embodiments are some embodiments of the present utility model, but not all embodiments of the present utility model. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model. It should be noted that, without conflict, the embodiments of the present utility model and features of the embodiments may be arbitrarily combined with each other.
In the description of the present utility model, it should also be noted that, unless explicitly specified and limited otherwise, the terms "disposed," "mounted," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; may be directly connected or indirectly connected through an intermediate medium. The specific meaning of the above terms in the present utility model will be understood in specific cases by those of ordinary skill in the art.
The utility model provides a slurry preparation system, which comprises: the first slurry part, the second slurry part, the third slurry part and the slurry tank. The first slurry part comprises a feed inlet, and is communicated with the water inlet pipeline to prepare slurry. The second slurry portion is in communication with the first slurry portion to store slurry formulated by the first slurry portion. The third sizing agent part is communicated with the second sizing agent part, and the sizing groove is communicated with the third sizing agent part so as to provide sizing agent for coating the warp yarn of the glass fiber electronic cloth. The ratio of the number of the first slurry part to the second slurry part is 1: the ratio of the number of the second slurry parts to the number of the third slurry parts is 1: m, wherein N and M are positive integers greater than or equal to 1. In the slurry preparation system of the present utility model, a large amount of slurry is prepared in the first slurry section, stored in each of the second slurry sections, and distributed to each of the third slurry sections. The primary batching can be supplied to a plurality of machines for use, so that the batching times are reduced; the first slurry part is discharged into the second slurry part in time after the first slurry part is mixed, the subsequent mixing operation is not influenced, the second slurry part supplements the slurry to the third slurry part in time, and the working efficiency is effectively improved. Meanwhile, the slurry preparation system can accurately control the water supplementing amount and the steam supply amount, and improves the quality stability of the slurry.
According to one exemplary embodiment, as shown in fig. 1, the present utility model provides a slurry formulation system, comprising: the first slurry section 100, the second slurry section 200, the third slurry section 300, the slurry tank 400, the first pipe 510, the second pipe 520, the third pipe 530, the water inlet pipe 600, the feed pipe 700, the steam pipe 800, and the waste liquid pipe 900.
As shown in fig. 1, the first slurry part 100 is respectively communicated with the water inlet pipe 600, the feed pipe 700 and the steam pipe 800 to quantitatively prepare the slurry required, and the first slurry part 100 is simultaneously communicated with the waste liquid pipe 900. The second slurry portion 200 is in communication with the first slurry portion 100 through the first pipe 510, the second slurry portion 200 is for storing slurry prepared by the first slurry portion 100, and the second slurry portion 200 is in communication with both the vapor pipe 800 and the waste liquid pipe 900. The third slurry portion 300 is in communication with the second slurry portion 200 via the second conduit 520, the third slurry portion 300 receives the slurry stored in the second slurry portion 200 for recycling, and the third slurry portion 300 is in communication with both the vapor conduit 800 and the waste conduit 900. The slurry tank 400 is communicated with the third slurry part 300 through a third pipeline 530, the slurry tank 400 is used for providing slurry for coating the glass fiber electronic cloth warp yarn, and the slurry tank 400 is simultaneously communicated with the waste liquid pipeline 900.
In the present embodiment, the ratio of the numbers of the first and second slurry portions 100 and 200 is one to one or more, and the ratio of the numbers of the second and third slurry portions 200 and 300 is one to one or more; after the first slurry section 100 completes the formulation, the slurry may be transferred to the plurality of second slurry sections 200, and then the first slurry section 100 continues to formulate the slurry. When the slurry is required for the plurality of third slurry portions 300, the slurry can be transported from the second slurry portion 200. Thus, the use efficiency of the first slurry part 100 is improved to the maximum extent, the third slurry part 300 is ensured to be continuously filled, and the slurry can be replenished into the slurry tank 400 at any time. The third slurry portions 300 are in one-to-one correspondence with the number of the slurry tanks 400, and the third slurry portions 300 are disposed above the slurry tanks 400, so that the slurry is directly discharged. The number of the second slurry part 200 and the third slurry part 300 is not particularly limited in the present utility model, and is set based on actual production requirements.
In actual use, in order to avoid deterioration of the slurry caused by too long a storage time of the slurry, the volume of the third slurry portion 300 may be set to be less than 1 ton so as to run out the slurry inside thereof in a short time; the volumes of the first slurry portion 100 and the second slurry portion 200 may be set to about 5 tons in order to improve the formulation efficiency.
As shown in fig. 2 and 3, the first slurry part 100 includes a first tank 110, a first stirring mechanism 120, a first heating mechanism 130, a weighing mechanism 140, a level gauge 150, and an insulation layer 160.
The first tank 110 is made of stainless steel to prevent the tank from corroding and rusting, and a feed inlet 111, a first liquid inlet 112 and a first liquid outlet 113 are formed in the first tank 110. As shown in fig. 2, a feed inlet 111 is provided at the top of the first tank 110, a feed pipe 700 and a steam pipe 800 are respectively communicated with the feed inlet 111, and a slurry raw material of the feed pipe 700 and steam of the steam pipe 800 enter the first tank 110 from the feed inlet 111; the first liquid inlet 112 is also arranged at the top of the first tank 110, and the preparation water of the water inlet pipeline 600 enters the first tank 110 from the first liquid inlet 112; within the first tank 110, the slurry material, steam, and the compounding water are mixed to formulate the desired slurry. The first liquid inlet 112 may also receive cleaning water required for cleaning the first tank 110, so as to facilitate cleaning of the first tank 110. The first liquid outlet 113 is disposed at the bottom of the first tank 110, and is used for delivering the prepared slurry to the second slurry portion 200 and delivering the waste liquid to the waste liquid pipeline 900.
In this embodiment, as shown in fig. 3, the first tank 110 further includes a drain branch 114 and a level switch 115. Specifically, the drainage branch 114 is disposed on the outlet pipeline of the first liquid outlet 113, and the waste liquid at the bottom of the first slurry portion 100 can be discharged into the waste liquid pipeline 900 through the drainage branch 114 and discharged through the drainage branch 114. The material level switch 115 is arranged at the outlet pipeline of the first liquid outlet 113, so that the automatic stop protection function can be realized when the first slurry part 100 is emptied and the empty tank appears, and the failure rate of equipment is reduced.
As shown in fig. 3, the first stirring mechanism 120 includes a first driving motor 121 and a first stirrer 122. The first driving motor 121 is disposed on the outside of the top of the first tank 110, the first stirrer 122 is disposed inside the first tank 110, and the first stirrer 122 is in driving connection with the first driving motor 121. The first agitator 122 may disperse and agitate the slurry uniformly under the driving of the first driving motor 121 to control the stability of the solid content of the slurry.
Returning to fig. 2, as shown in fig. 2, the first heating mechanism 130 includes a first heating coil 131 and a first heater 132. The first heating coil 131 is disposed on the inner wall of the first tank 110, the first heater 132 is electrically connected to the first heating coil 131, and the first heating coil 131 is in communication with the steam line 800 to heat the steam to control the temperature in the first slurry portion 100. The first heater 132 may use a thermocouple through which the heating temperature is detected and controlled.
As shown in fig. 3, a weighing mechanism 140 is provided at the bottom of the first tank 110, and the weighing mechanism 140 prompts the system to display an error when the input slurry material or the discharged formulation water exceeds a set weight range. The stock of slurry in the first slurry portion 100 can also be known by the weighing mechanism 140, which provides a basis for the subsequent formulation of the slurry.
As shown in fig. 3, the liquid level meter 150 is disposed on the side wall of the first tank 110, and a high liquid level alarm switch (not shown in the drawing) is further disposed on the liquid level meter 150, so that the liquid level meter 150 can monitor the actual liquid level condition in the tank through the arrangement on the touch screen, and the high liquid level alarm switch performs a protection function.
Returning to fig. 2, as shown in fig. 2, the heat-insulating layer 160 is disposed on the inner wall of the first tank 110, and the heat-insulating material in the heat-insulating layer 160 may be perlite heat-insulating filler, so as to reduce heat dissipation in the tank, so as to maintain the stability of the slurry temperature in the tank and reduce the fluctuation of the slurry temperature.
In this embodiment, the second slurry portion 200 and the third slurry portion 300 have the same structure as the first slurry portion 100, and have the structures of a tank, a stirring mechanism, a heating mechanism, a weighing mechanism, a level gauge, an insulating layer, and the like, and the structures are the same and will not be described again. The difference is that the second tank body of the second slurry portion 200 is not provided with a feed inlet, and the second liquid inlet is used for receiving the slurry conveyed by the first slurry portion 100; similarly, the third tank of the third slurry portion 300 is not provided with a feed port, and the third feed port is used for receiving the slurry conveyed by the second slurry portion 200.
In some other embodiments, the second slurry portion 200 and the third slurry portion 300 may be configured identically to the first slurry portion 100, the second inlet of the second tank receives the slurry delivered by the first slurry portion 100, and the third inlet of the third tank receives the slurry delivered by the second slurry portion 200. The three slurry parts have the same structure, so that the manufacturing cost is reduced, and the mass production is facilitated. The second liquid inlet of the second tank and the third liquid inlet of the third tank in this embodiment may be respectively communicated with the water inlet pipe 600, and when the slurry in the second slurry portion 200 and the third slurry portion 300 is left standing for too long to raise the solid content of the slurry, the solid content of the slurry may be kept stable by directly introducing quantitative water.
As shown in fig. 1, a centrifugal pump 540 and a pneumatic ball valve 550 are sequentially provided on the first, second and third pipelines 510, 520 and 530, respectively. The centrifugal pump 540 and the pneumatic ball valve 550 are used for conveying slurry, when the slurry is required to be conveyed, the pneumatic ball valve 550 is opened, and the centrifugal pump 540 starts to work; when slurry is not needed, the pneumatic ball valve 550 is closed and the centrifugal pump 540 stops. By providing a centrifugal pump 540 and a pneumatic ball valve 550, control of the slurry delivery line is enhanced, making the adjustment of the slurry formulation system of the present utility model more flexible.
A water inlet valve 610 is provided on the line of the water inlet line 600 leading to the first slurry part 100, and the water inlet valve 610 is used for controlling the amount of water entering the feed inlet 111.
The pipes of the steam pipe 800 leading to the first slurry part 100, the second slurry part 200 and the third slurry part 300 are respectively provided with a pneumatic high-temperature angle seat valve 810, and the pneumatic high-temperature angle seat valve 810 is used for accurately controlling the supply amount of steam, so that the control precision of the slurry temperature is improved.
The waste liquid pipeline 900 is provided with a waste liquid control valve 910, and the waste liquid control valve 910 may be specifically disposed on each pipeline of the first slurry portion 100, the second slurry portion 200, the third slurry portion 300, and the slurry tank 400, which are in communication with the waste liquid pipeline 900, to control the discharge amount of the waste liquid. It should be noted that, in the present embodiment, the third slurry portion 300 may be directly connected to the waste liquid pipeline 900 through the third liquid outlet thereof, and in some other embodiments, the third slurry portion 300 may also be connected to the waste liquid pipeline 900 by using the liquid outlet of the slurry tank 400, and the third slurry portion 300 itself is not directly connected to the waste liquid pipeline 900, so as to simplify the structural arrangement of the system pipeline.
The slurry preparation system of the present utility model further includes a control unit (not shown), and the control unit may be a PLC system (Programmable Logic Controller ). The first slurry section 100, the second slurry section 200, the third slurry section 300, and the slurry tank 400 are electrically connected to a control section that automatically operates the dispensing apparatus. Specifically, the control part is respectively and electrically connected with the driving motor, the heating coil, the high liquid level alarm switch, the material level switch, the centrifugal pump 540, the pneumatic ball valve 550, the water inlet valve 610, the pneumatic high-temperature angle seat valve 810 and the waste liquid control valve 910, and the control part ensures accurate supply of water and steam through control of the pipeline valve, ensures stable quality of slurry and improves the automation level of the system.
In summary, in the slurry preparation system of the present utility model, a certain amount of preparation water is discharged into the first slurry part 100 through the water inlet line 600, and simultaneously, the preparation water is heated to a designated temperature through the steam line 800, and after being prepared into a slurry with other raw materials, the slurry is transferred to the second slurry part 200 for temporary storage. The emptied first slurry portion 100 may continue to prepare slurry. When the replenishment of the paste is required in the third paste portion 300, the paste may be discharged from the second paste portion 200, and the paste tank 400 communicates with the third paste portion 300 to provide the paste for coating the glass fiber electronic cloth warp yarns. The slurry preparation system improves the product quality and improves the preparation efficiency of the slurry.
Finally, it should be noted that: the above embodiments are only for illustrating the technical scheme of the present utility model, and are not limited thereto. Although the utility model has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit of the corresponding technical solutions from the scope of the technical solutions of the embodiments of the present disclosure.

Claims (10)

1. A slurry formulation system, the slurry formulation system comprising: the first slurry part, the second slurry part, the third slurry part and the slurry tank;
the first slurry part comprises a feed inlet, and is communicated with a water inlet pipeline to prepare slurry; the second slurry part is communicated with the first slurry part so as to store the slurry prepared by the first slurry part;
the third slurry part is communicated with the second slurry part;
the slurry tank is communicated with the third slurry part to provide slurry for coating the warp of the glass fiber electronic cloth;
the ratio of the number of the first slurry part to the number of the second slurry part is 1: n, the ratio of the number of the second slurry portions to the number of the third slurry portions is 1: m, wherein N and M are positive integers greater than or equal to 1.
2. The slurry formulation system of claim 1, wherein the slurry is,
the third slurry parts are in one-to-one correspondence with the number of the slurry tanks, and the third slurry parts are arranged above the slurry tanks.
3. The slurry formulation system of claim 1, wherein the slurry is,
the first slurry portion includes: the device comprises a first tank body, a first stirring mechanism and a first heating mechanism; the feed inlet is arranged on the first tank body; the first tank body further comprises a first liquid inlet and a first liquid outlet;
the first stirring mechanism comprises a first stirrer, and the first stirrer is arranged in the first tank body;
the first heating mechanism comprises a first heating coil and a first heater, the first heating coil is arranged on the inner wall of the first tank body, and the first heater is electrically connected with the first heating coil.
4. The slurry formulation system of claim 3, wherein,
the second slurry portion includes: the second tank body, the second stirring mechanism and the second heating mechanism; the second tank body further comprises a second liquid inlet and a second liquid outlet; the second liquid outlet is communicated with the first liquid outlet;
the second stirring mechanism comprises a second stirrer, and the second stirrer is arranged in the second tank body;
the second heating mechanism comprises a second heating coil pipe and a second heater, the second heating coil pipe is arranged on the inner wall of the second tank body, and the second heater is electrically connected with the second heating coil pipe;
the third slurry includes: a third tank, a third stirring mechanism and a third heating mechanism; the third tank body further comprises a third liquid inlet and a third liquid outlet; the third liquid outlet is communicated with the second liquid outlet;
the third stirring mechanism comprises a third stirrer, and the third stirrer is arranged in the third tank body;
the third heating mechanism comprises a third heating coil and a third heater, the third heating coil is arranged on the inner wall of the third tank body, and the third heater is electrically connected with the third heating coil.
5. The slurry formulation system of claim 4, wherein the first slurry portion, the second slurry portion, and the third slurry portion further comprise:
the weighing mechanism is respectively arranged at the bottoms of the first tank body, the second tank body and/or the third tank body.
6. The slurry formulation system of claim 4, wherein the first slurry portion, the second slurry portion, and the third slurry portion further comprise:
the liquid level meter is arranged on the side wall of the first tank body, the second tank body and/or the third tank body.
7. The slurry formulation system of claim 4, wherein the slurry is,
and the first liquid outlet, the second liquid outlet and the third liquid outlet are respectively provided with a material level switch.
8. The slurry formulation system of claim 4, wherein the first slurry portion, the second slurry portion, and the third slurry portion further comprise:
the heat preservation layer is arranged on the inner walls of the first tank body, the second tank body and/or the third tank body respectively.
9. The slurry formulation system of claim 4, wherein the slurry is,
the slurry preparation system also comprises a feeding pipeline and a steam pipeline;
the feeding pipeline and the steam pipeline are respectively communicated with the feeding port;
the steam pipeline is respectively communicated with the first liquid inlet, the second liquid inlet and the third liquid inlet.
10. The slurry formulation system of claim 4, wherein the slurry is,
the slurry preparation system further comprises a waste liquid pipeline which is respectively communicated with the first liquid outlet, the second liquid outlet and the third liquid outlet.
CN202320849744.5U 2023-04-12 2023-04-12 Slurry preparation system Active CN219930476U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202320849744.5U CN219930476U (en) 2023-04-12 2023-04-12 Slurry preparation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202320849744.5U CN219930476U (en) 2023-04-12 2023-04-12 Slurry preparation system

Publications (1)

Publication Number Publication Date
CN219930476U true CN219930476U (en) 2023-10-31

Family

ID=88486881

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202320849744.5U Active CN219930476U (en) 2023-04-12 2023-04-12 Slurry preparation system

Country Status (1)

Country Link
CN (1) CN219930476U (en)

Similar Documents

Publication Publication Date Title
JP3176624B2 (en) Equipment for mixing and dispensing of chemical concentrates
CN102527269A (en) Continuous production process and equipment for liquid detergent
CN219930476U (en) Slurry preparation system
US3570717A (en) System for fluent material dispensing with electrical controls
CN107029622A (en) Urethane raw high-precision measuring mixing equipment
CN210410306U (en) Dye auxiliary agent chemical material distribution device
CN201148408Y (en) Multi-kettle continuous production apparatus for waterborne polyurethane polymerization reaction
CN206810192U (en) Urethane raw high-precision measuring mixing equipment
CN206810232U (en) A kind of automation charging control system for preparing iminodisuccinic acid
CN202478933U (en) Continuous production equipment for liquid detergent
CN113117584A (en) Automatic auxiliary agent distribution device and distribution method thereof
CN212955943U (en) Automatic change quantitative feeding device
CN208818313U (en) Feed proportioning system is sent for producing the automatic of PVC pharmaceutical pack piece
CN108277032A (en) A kind of equipment of producing modified asphalt
CN211105746U (en) Injection filling and glue injecting machine for multi-resin pultrusion
CN209123834U (en) A kind of glue preparation production system
CN220907123U (en) Canned feed liquid conveying system
CN112403387A (en) Comprehensive sizing material circulating system
GB2338658A (en) Computer-controlled apparatus for the manufacture and distribution of slurry
CN212369955U (en) Large amount of powder auxiliary agent standard liquid form storage and distribution system
CN217678195U (en) Liquefaction device for powder washing products
CN218307732U (en) Full-automatic proportioning device for washing and protecting articles
CN214915166U (en) Intelligent compounding device for circulating water quality stabilizer
CN211612531U (en) Spinning emulsion modulating system
CN217568560U (en) Intelligent additive adding and stirring system for asphalt station

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant