CN205550169U - Washing powder production system with waste recycling function - Google Patents
Washing powder production system with waste recycling function Download PDFInfo
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- CN205550169U CN205550169U CN201620129149.4U CN201620129149U CN205550169U CN 205550169 U CN205550169 U CN 205550169U CN 201620129149 U CN201620129149 U CN 201620129149U CN 205550169 U CN205550169 U CN 205550169U
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- branch road
- discharging
- discharging branch
- filter
- ageing
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Abstract
The utility model relates to a washing powder production system with waste recycling function, it is connected with solid material interpolation branch road (11), liquid material interpolation branch road (12), circulates and retrieve branch road (13) and ejection of compact branch road A (14) including prepare burden jar (1), filter (2), recovery agitator tank (3), ageing can (4), spray tower (5) and control system (6) on prepare burden jar (1), batching jar (1) be connected with filter (2) through ejection of compact branch road A (14), filter (2) still respectively through ejection of compact branch road B (21) and ejection of compact branch road C (22) with retrieve agitator tank (3) and ageing can (4) and be connected, recovery agitator tank (3) retrieve branch road (13) through the circulation and be connected with batching jar (1), ageing can (4) be connected with spray tower (5) through ejection of compact branch road D (41). The utility model has the advantages of utilization ratio of material, reduction in production cost can be effectively improved, environmental pollution is alleviateed.
Description
Technical field
This utility model relates to detergent process units technical field, a kind of production system of washing powder with waste recovery function.
Background technology
Detergent is articles for washing conventional in people's daily life.The advantages such as compared with the articles for washing such as soap, liquid detergent, it is good, easy to use that it has strong detergency, solubility property, and price is cheap, the most even better at aspects such as hard water resistance, foaming abundancy, it is the laundry detergent that a kind of cost performance is higher.
At present, the domestic conventional detergent technological process of production mostly is high tower powder injection process flow process, and its technological process is as follows: first, mixes in being transported to material-compound tank after various solid materials and liquid charging stock being weighed, and reaction obtains the slip that water content is about 36%；Then, slip is filtered in ageing can sent into by rear gained fines aging；Final after Homogenizing pump grinds further, sprayed into drying and moulding in spray tower by high-pressure pump the most again.In above-mentioned steps, after slip is filtered, follow-up aging and high tower powder injection process will certainly being cannot be introduced into by the block and oarse-grained detergent of residual fraction, if it directly being abandoned, not only wasting raw materials for production, also surrounding can be brought certain harm simultaneously.
Utility model content
The purpose of this utility model is to overcome the shortcoming of prior art, it is provided that a kind of can improve raw material availability, save production cost and can reduce again the production system of washing powder with waste recovery function of environmental pollution.
nullThe purpose of this utility model is achieved through the following technical solutions: a kind of production system of washing powder with waste recovery function，It includes material-compound tank、Filter、Reclaim agitator tank、Ageing can、Spray tower and control system，Connect on described material-compound tank and have solid material to add branch road、Liquid material adds branch road、Circulation and stress branch road and discharging branch road A，Described material-compound tank is connected with filter by discharging branch road A，Described filter is connected with recovery agitator tank and ageing can by discharging branch road B and discharging branch road C the most respectively，Described recovery agitator tank is connected with material-compound tank by circulation and stress branch road，Described ageing can is connected with spray tower by discharging branch road D，Agitating device it is provided with respectively on described material-compound tank and recovery agitator tank，Described solid material adds branch road、Liquid material adds branch road、Circulation and stress branch road、Discharging branch road A、Filter、Discharging branch road B、Discharging branch road C、Discharging branch road D、Spray tower and agitating device are all connected with control system.
Preferably, described solid material interpolation branch road and liquid material interpolation branch road being provided with weigher, described weigher is connected with control system.
Preferably, described solid material interpolation branch road, liquid material interpolation branch road, circulation and stress branch road, discharging branch road A, discharging branch road B, discharging branch road C and discharging branch road D being provided with valve, described valve is connected with control system.
Preferably, described control system includes timing module and signal processing module, described timing module is connected with the input of signal processing module, and the outfan of described signal processing module adds branch road with solid material respectively, liquid material is added branch road, circulation and stress branch road, discharging branch road A, filter, discharging branch road B, discharging branch road C, discharging branch road D, spray tower and agitating device and is connected.
This utility model has the advantage that
1, improve raw material availability, save production cost, reduce environmental pollution: this utility model is by filter and material-compound tank, between circulation stirring tank be set achieve the recycling to bulky grain detergent, avoid the wasting of resources and the problem of environmental pollution directly block or bulky grain detergent caused directly as waste disposal in traditional processing technology flow process, while improving resource utilization, saving production cost, decrease environmental pollution.
2, automaticity is high: be provided with control system in this utility model, can be to the opening and closing of valve on branch road each in production system, material adds time, addition, material efflux time, mixings time etc. automatically control, and reduce workman's amount of labour, save labour cost while improving automation degree of equipment, avoiding the mistake that manual operation brings, production run is more safe and reliable.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
In figure: 1-material-compound tank, 11-expects to add branch road admittedly, and 12-liquid material adds branch road, 13-circulation and stress branch road, 14-discharging branch road A, 2-filter, 21-discharging branch road B, 22-discharging branch road C, 3-reclaim agitator tank, 4-ageing can, 41-discharging branch road D, 5-spray tower, 6-control system, 7-agitating device, 8-weigher.
Detailed description of the invention
Below in conjunction with the accompanying drawings this utility model is further described, but protection domain of the present utility model is not limited to the following stated.
As it is shown in figure 1, a kind of production system of washing powder with waste recovery function, it includes material-compound tank 1, filter 2, reclaims agitator tank 3, ageing can 4, spray tower 5 and control system 6.
Connect on described material-compound tank 1 and have solid material to add branch road 11, liquid material interpolation branch road 12, circulation and stress branch road 13 and discharging branch road A14.Described material-compound tank 1 is connected with filter 2 by discharging branch road A14, described filter 2 is connected with recovery agitator tank 3 and ageing can 4 by discharging branch road B21 and discharging branch road C22 the most respectively, described recovery agitator tank 3 is connected with material-compound tank 1 by circulation and stress branch road 13, and described ageing can 4 is connected with spray tower 5 by discharging branch road D41.It is provided with respectively on described material-compound tank 1 and recovery agitator tank 3 on agitating device 7, described solid material interpolation branch road 11 and liquid material interpolation branch road 12 and is provided with weigher 8.
Being provided with valve on described solid material interpolation branch road 11, liquid material interpolation branch road 12, circulation and stress branch road 13, discharging branch road A14, discharging branch road B21, discharging branch road C22 and discharging branch road D41, all above valve, filter 2, spray tower 5, agitating device 7 and weigher 8 are all connected with control system 6.
Described control system 6 includes timing module and signal processing module, described timing module is connected with the input of signal processing module, and the outfan of described signal processing module is connected with all above valve, filter 2, spray tower 5, agitating device 7 and weigher 8 respectively.Control system 6 can be to the opening and closing of all above valve, and material adds time, addition, material efflux time, and mixing time etc. automatically controls, and automaticity is high, and production safety is reliable.
Work process of the present utility model is as follows: first, and various solid materials and liquid charging stock mix in being transported to material-compound tank 1 by solid material interpolation branch road 11 and liquid material interpolation branch road 12 respectively after weighing, and reaction prepares the slip with certain water content；Then, slip fines of gained after filter 2 filters is aging in sending into ageing can 4；Final after Homogenizing pump grinds further, sprayed into drying and moulding in spray tower 5 by high-pressure pump the most again；Block or bulky grain detergent returns material-compound tank 1 after being stirred refinement in then entering recovery agitator tank 3 and is continuing with.
Claims (4)
- null1. a production system of washing powder with waste recovery function，It is characterized in that: it includes material-compound tank (1)、Filter (2)、Reclaim agitator tank (3)、Ageing can (4)、Spray tower (5) and control system (6)，The upper connection of described material-compound tank (1) has solid material to add branch road (11)、Liquid material adds branch road (12)、Circulation and stress branch road (13) and discharging branch road A(14)，Described material-compound tank (1) passes through discharging branch road A(14) it is connected with filter (2)，Described filter (2) is the most respectively by discharging branch road B(21) and discharging branch road C(22) be connected with recovery agitator tank (3) and ageing can (4)，Described recovery agitator tank (3) is connected with material-compound tank (1) by circulation and stress branch road (13)，Described ageing can (4) passes through discharging branch road D(41) it is connected with spray tower (5)，Agitating device (7) it is provided with respectively on described material-compound tank (1) and recovery agitator tank (3)，Described solid material adds branch road (11)、Liquid material adds branch road (12)、Circulation and stress branch road (13)、Discharging branch road A(14)、Filter (2)、Discharging branch road B(21)、Discharging branch road C(22)、Discharging branch road D(41)、Spray tower (5) and agitating device (7) are all connected with control system (6).
- A kind of production system of washing powder with waste recovery function the most according to claim 1, it is characterized in that: being provided with weigher (8) on described solid material interpolation branch road (11) and liquid material interpolation branch road (12), described weigher (8) is connected with control system (6).
- A kind of production system of washing powder with waste recovery function the most according to claim 1, it is characterized in that: described solid material adds branch road (11), liquid material adds branch road (12), circulation and stress branch road (13), discharging branch road A(14), discharging branch road B(21), discharging branch road C(22) and discharging branch road D(41) on be provided with valve, described valve is connected with control system (6).
- A kind of production system of washing powder with waste recovery function the most according to claim 1, it is characterized in that: described control system (6) includes timing module and signal processing module, described timing module is connected with the input of signal processing module, the outfan of described signal processing module adds branch road (11) with solid material respectively, liquid material adds branch road (12), circulation and stress branch road (13), discharging branch road A(14), filter (2), discharging branch road B(21), discharging branch road C(22), discharging branch road D(41), spray tower (5) and agitating device (7) connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620129149.4U CN205550169U (en) | 2016-02-19 | 2016-02-19 | Washing powder production system with waste recycling function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620129149.4U CN205550169U (en) | 2016-02-19 | 2016-02-19 | Washing powder production system with waste recycling function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205550169U true CN205550169U (en) | 2016-09-07 |
Family
ID=56817955
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620129149.4U Expired - Fee Related CN205550169U (en) | 2016-02-19 | 2016-02-19 | Washing powder production system with waste recycling function |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205550169U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109999746A (en) * | 2019-05-10 | 2019-07-12 | 海安艾拉新材料有限公司 | Solid-liquid circular response device |
-
2016
- 2016-02-19 CN CN201620129149.4U patent/CN205550169U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109999746A (en) * | 2019-05-10 | 2019-07-12 | 海安艾拉新材料有限公司 | Solid-liquid circular response device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160907 Termination date: 20210219 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |