CN204182620U - Energy-saving full-automatic cleaning station - Google Patents
Energy-saving full-automatic cleaning station Download PDFInfo
- Publication number
- CN204182620U CN204182620U CN201420638524.9U CN201420638524U CN204182620U CN 204182620 U CN204182620 U CN 204182620U CN 201420638524 U CN201420638524 U CN 201420638524U CN 204182620 U CN204182620 U CN 204182620U
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- Prior art keywords
- cleaning
- control element
- tank
- plc control
- cleaning station
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- 238000004140 cleaning Methods 0.000 title claims abstract description 91
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000003513 alkali Substances 0.000 claims abstract description 18
- 238000010992 reflux Methods 0.000 claims abstract description 18
- 239000000178 monomer Substances 0.000 claims abstract description 17
- 238000005406 washing Methods 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims description 11
- 239000010865 sewage Substances 0.000 claims description 6
- 230000003139 buffering effect Effects 0.000 claims description 4
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 239000000126 substance Substances 0.000 abstract description 10
- 230000002000 scavenging effect Effects 0.000 abstract description 5
- 238000011084 recovery Methods 0.000 abstract 1
- 239000012530 fluid Substances 0.000 description 10
- 238000003860 storage Methods 0.000 description 9
- 239000007788 liquid Substances 0.000 description 5
- 235000013361 beverage Nutrition 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 235000013365 dairy product Nutrition 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000021715 photosynthesis, light harvesting Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
Landscapes
- Cleaning By Liquid Or Steam (AREA)
Abstract
The utility model discloses energy-saving full-automatic cleaning station, cleaning station has: PLC control element; Sequentially be installed on access pipeline and be provided with by the sour tank interface of Valve controlling, alkali tank interface, recovery water pot interface, clean water tank interface; Be connected to access pipeline and the booster pump be connected with PLC control element; Be connected to the heat exchanger of booster pump, the output of heat exchanger is connected to washing outlet, and heat exchanger is provided with steam control valve, and washing outlet is provided with the valve controlled by PLC control element; Cleaning station has the cleaning return port being connected to cleaning object, cleaning return port is provided with the valve controlled by PLC control element, cleaning return port is connected to monomer circulating tank, and monomer circulating tank is provided with sour tank refluxing opening, alkali tank refluxing opening, reclaims water pot refluxing opening; Monomer circulating tank is connected with booster pump, heat exchanger; The reflux pipeline of cleaning station is provided with the online temperature monitor be connected with PLC control element respectively, online conductivity meter.This cleaning station can save steam consumption and chemicals and scavenging period greatly.
Description
Technical field
The utility model relates to liquid milk/beverage production device, especially relates to a kind of energy-saving full-automatic cleaning station.
Background technology
Along with the extensive development that dairy beverage is produced, domestic manufacturer improves for the requirement of equipment washing and sterilizing thereupon, and existing equipment there is no method and satisfies the demands.
Specifically, the consumption that conventional CIP stands in steam cannot provide according to actual needs, cause the increase of energy consumption, and the consumption of chemicals and scavenging period are all not fully up to expectations.
Utility model content
The purpose of this utility model is exactly to solve the problem, and provides one can cleaning fluid needed for heat cycles according to actual needs, and effectively can save the energy-saving full-automatic cleaning station of chemicals and scavenging period.
To achieve these goals, the utility model adopts following technical scheme:
Energy-saving full-automatic cleaning station, is characterized in that, this cleaning station has:
PLC control element;
Sequentially be installed on the sour tank interface (A) of access pipeline (2), alkali tank interface (B), reclaim water pot interface (C), clean water tank interface (D), this access pipeline has the sewage draining exit (E) controlled by by-pass valve control, and described sour tank interface, alkali tank interface, return water pipe interface, clean water tank interface, sewage outfalls setting have the valve controlled by PLC control element;
Be connected to the booster pump (3) of access pipeline, it is connected to PLC control element;
Be connected to the heat exchanger (4) of booster pump, the output of this heat exchanger is connected to washing outlet (6), and this heat exchanger is provided with steam control valve (5), and washing outlet is provided with the valve controlled by PLC control element;
This cleaning station has the cleaning return port (7) being connected to cleaning object, described cleaning return port is provided with the valve controlled by PLC control element, described cleaning return port is connected to the monomer circulating tank (1) playing buffering and exhaust operation in cleaning process, and described monomer circulating tank is provided with sour tank refluxing opening (A '), alkali tank refluxing opening (B '), reclaims water pot refluxing opening (C ');
Wherein, described monomer circulating tank is connected with booster pump, heat exchanger;
The reflux pipeline of this cleaning station is provided with the online temperature monitor be connected with PLC control element respectively, online conductivity meter.
Described washing outlet place is provided with the ratio adjusting valve regulated temperature.
The frequency converter that the export pipeline of this cleaning station is provided with online flowmeter (8) and is connected with online flowmeter, this frequency converter, online flowmeter are connected to PLC control element.
Described PLC control element is connected to man-machine interface.
The utility model has following beneficial effect:
(1) reduce the loss of chemicals, reduce the impact to environment, accurately control the faying face of chemicals and water, reduce mixing section, thus reduce chemical cost; By-pass valve control is integrated in a frame by this patent, improves the valve scattered distribution of original system, thus greatly reduces the mixing section of chemicals and water, and according to the difference of each factory cleaning frequency, chemicals loss can reduce 5-15%;
(2) the steam power consumption of each cleaning fluid heating is saved; Original system needs to carry out preheating to the cleaning fluid of whole storage tank before cleaning, and the capacity of whole storage tank is generally 2000-20000 and does not rise not etc., but the reality internal circulating load required when clear each object is usually less than the half of tank capacity, even only have about 10%, the monomer circulating tank of this patent design, make in cleaning process, can only need heating to participate in the part liquid of clean cycle, thus greatly shorten the heat time of cleaning and the steam energy required for heated wash liquid;
(3) this four large key parameter of temperature, concentration, cleaning flow and scavenging period is monitored, a qualified cleaning process must meet a little great purge key element, temperature, concentration, flow velocity, time, the outlet temperature passing ratio control valve of this product to cleaning regulates, outlet temperature can be made to remain in the temperature of user's setting, reflux pipeline has been installed online temperature monitor, cleaning reflux temperature is monitored, what temperature did not reach requirement is not counted in the normal wash time, equally the cleaning concentration of cleaning backflow is also monitored by online conductivity meter, what do not reach cleaning requirement is not counted in the normal wash time, for the control of flow, this patent has set up an online flowmeter and frequency converter composition closed-loop adjustment loop, cleaning flow can be remained on the range of flow of setting, in addition, because the equipment of a factory is varied, for different equipment, key process parameter during cleaning requires different, and this patent makes the key process parameter of each cleaning object to set separately, does not respectively affect.
Accompanying drawing explanation
Fig. 1 is energy-saving full-automatic cleaning station front view.
Fig. 2 is energy-saving full-automatic cleaning station side view.
Fig. 3 is energy-saving full-automatic cleaning station top view.
Detailed description of the invention
The technological means realized to make the utility model, creation characteristic, reaching object and effect is easy to understand, below in conjunction with specific embodiment, setting forth the utility model further.
As Figure 1-3, energy-saving full-automatic cleaning station, this cleaning station has: be connected to the PLC control element of man-machine interface, booster pump, heat exchanger, monomer circulating tank.
Wherein, monomer circulating tank just comes into operation in cleaning process, play the effect of buffering and exhaust, for the application that some cleaning flows are more stable, when cleaning fluid confesses cleaning object from storage tank, and after being back to cleaning station from cleaning object, do not enter cleaning fluid storage tank, but enter the little a lot of monomer circulating tank of volume, set up monomer circulating tank and the direct closed circulation of cleaning object, for the Cleaning application that some flowed fluctuations are very large, this patent is provided with transfer valve group and makes it possible to directly set up circulation at cleaning fluid storage tank and cleaning object, solve the control difficult problem that flow wide fluctuations is brought.
Sequentially be installed on sour tank interface A, the alkali tank interface B of access pipeline 2, reclaim water pot interface C, clean water tank interface D, this access pipeline has the sewage draining exit E controlled by by-pass valve control, and described sour tank interface, alkali tank interface, return water pipe interface, clean water tank interface, sewage outfalls setting have the valve controlled by PLC control element.
Be connected to the booster pump 3 of access pipeline, it is connected to PLC control element.
Be connected to the heat exchanger 4 of booster pump, the output of this heat exchanger is connected to washing outlet 6, and this heat exchanger is provided with steam control valve 5, and washing outlet is provided with the valve controlled by PLC control element.
This cleaning station has the cleaning return port 7 being connected to cleaning object, described cleaning return port is provided with the valve controlled by PLC control element, described cleaning return port is connected to the monomer circulating tank 1 playing buffering and exhaust operation in cleaning process, and described monomer circulating tank is provided with sour tank refluxing opening A ', alkali tank refluxing opening B ', reclaims water pot refluxing opening C '.
Wherein, described monomer circulating tank is connected with booster pump, heat exchanger.
The reflux pipeline of this cleaning station is provided with the online temperature monitor be connected with PLC control element respectively, online conductivity meter, and figure 3 illustrates the installation position K of flow switch, online conductivity meter, thermometer, in this installation position, K installs corresponding instrument.
Described washing outlet place is provided with the ratio adjusting valve regulated temperature.
The frequency converter that the export pipeline of this cleaning station is provided with online flowmeter 8 and is connected with online flowmeter, this frequency converter, online flowmeter are connected to PLC control element.
For alkali cleaning, cleaning process is described below:
The first step is filled
Alkali liquor storage tank-booster pump-heat exchanger-cleaning object-circulating tank;
Second step clean cycle
Circulating tank-booster pump-heat exchanger-cleaning object-circulating tank;
3rd step cleaning fluid reclaims
Circulating tank-booster pump-heat exchanger-cleaning object-alkali liquor storage tank;
And the alkali cleaning flow process of routine is: alkali liquor storage tank-booster pump-heat exchanger-cleaning object-alkali liquor storage tank.
The CIP station of conventional type needs whole tank liquid to be heated to required cleaning temperature (being generally 65-85 degree) from normal temperature, then could effectively clean, if the cleaning frequency is not high, the cleaning fluid so heated can slowly cool again, and energy dissipation in the environment; And novel CIP station is owing to establishing a little circulating system, cleans at every turn, only need the cleaning fluid needed for heat cycles, be generally a few hectolitre, greatly can save the consumption of steam like this.
Stand relative to conventional type CIP, novel C IP station concentrates on valve in a unit, effectively decrease the mixing of acid & alkali liquid and cleaning fluid, thus reduce the chemical cost of each cleaning, and faster intrasystem residual chemical can be rinsed well, thus save consumption and the scavenging period of water.
The foregoing is only preferred embodiment of the present utility model, protection domain of the present utility model is not limited in above-mentioned embodiment, and every technical scheme belonging to the utility model principle all belongs to protection domain of the present utility model.For a person skilled in the art, the some improvement carried out under the prerequisite not departing from principle of the present utility model, these improvement also should be considered as protection domain of the present utility model.
Claims (4)
1. energy-saving full-automatic cleaning station, is characterized in that, this cleaning station has:
PLC control element;
Sequentially be installed on the sour tank interface (A) of access pipeline (2), alkali tank interface (B), reclaim water pot interface (C), clean water tank interface (D), this access pipeline has the sewage draining exit (E) controlled by by-pass valve control, and described sour tank interface, alkali tank interface, return water pipe interface, clean water tank interface, sewage outfalls setting have the valve controlled by PLC control element;
Be connected to the booster pump (3) of access pipeline, it is connected to PLC control element;
Be connected to the heat exchanger (4) of booster pump, the output of this heat exchanger is connected to washing outlet (6), and this heat exchanger is provided with steam control valve (5), and washing outlet is provided with the valve controlled by PLC control element;
This cleaning station has the cleaning return port (7) being connected to cleaning object, described cleaning return port is provided with the valve controlled by PLC control element, described cleaning return port is connected to the monomer circulating tank (1) playing buffering and exhaust operation in cleaning process, and described monomer circulating tank is provided with sour tank refluxing opening (A '), alkali tank refluxing opening (B '), reclaims water pot refluxing opening (C ');
Wherein, described monomer circulating tank is connected with booster pump, heat exchanger;
The reflux pipeline of this cleaning station is provided with the online temperature monitor be connected with PLC control element respectively, online conductivity meter.
2. energy-saving full-automatic cleaning station according to claim 1, is characterized in that, described washing outlet place is provided with the ratio adjusting valve regulated temperature.
3. energy-saving full-automatic cleaning station according to claim 1, it is characterized in that, the frequency converter that the export pipeline of this cleaning station is provided with online flowmeter (8) and is connected with online flowmeter, this frequency converter, online flowmeter are connected to PLC control element.
4. energy-saving full-automatic cleaning station according to claim 1, is characterized in that, described PLC control element is connected to man-machine interface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420638524.9U CN204182620U (en) | 2014-10-30 | 2014-10-30 | Energy-saving full-automatic cleaning station |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420638524.9U CN204182620U (en) | 2014-10-30 | 2014-10-30 | Energy-saving full-automatic cleaning station |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204182620U true CN204182620U (en) | 2015-03-04 |
Family
ID=52614651
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420638524.9U Active CN204182620U (en) | 2014-10-30 | 2014-10-30 | Energy-saving full-automatic cleaning station |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204182620U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105750260A (en) * | 2016-05-10 | 2016-07-13 | 北京瀚海峰科技有限公司 | CIP cleaning liquid recovering equipment and cleaning system based on same |
| CN108687027A (en) * | 2018-05-17 | 2018-10-23 | 杭州娃哈哈精密机械有限公司 | Energy-saving CIP automatic cleaning systems with pneumatic jack soda acid technology |
| CN110404869A (en) * | 2019-08-12 | 2019-11-05 | 陆阳清 | A kind of cleaning method and cleaning equipment of solar energy silicon crystal slate |
-
2014
- 2014-10-30 CN CN201420638524.9U patent/CN204182620U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105750260A (en) * | 2016-05-10 | 2016-07-13 | 北京瀚海峰科技有限公司 | CIP cleaning liquid recovering equipment and cleaning system based on same |
| CN108687027A (en) * | 2018-05-17 | 2018-10-23 | 杭州娃哈哈精密机械有限公司 | Energy-saving CIP automatic cleaning systems with pneumatic jack soda acid technology |
| CN110404869A (en) * | 2019-08-12 | 2019-11-05 | 陆阳清 | A kind of cleaning method and cleaning equipment of solar energy silicon crystal slate |
| CN110404869B (en) * | 2019-08-12 | 2020-11-10 | 江苏润祁项目管理有限公司 | Cleaning method and cleaning equipment for solar silicon crystal plate |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201202 Address after: 201199 Room 101, building 7, block B, No. 237, Youdong Road, Minhang District, Shanghai Patentee after: Shanghai helim Food Machinery Equipment Co.,Ltd. Address before: 200231, room 8, No. 259, Lane 401, waiting Road, Xuhui District, Shanghai Patentee before: Min Jianping |