CN204624370U - Fluid material automation storage device - Google Patents
Fluid material automation storage device Download PDFInfo
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- CN204624370U CN204624370U CN201520192227.0U CN201520192227U CN204624370U CN 204624370 U CN204624370 U CN 204624370U CN 201520192227 U CN201520192227 U CN 201520192227U CN 204624370 U CN204624370 U CN 204624370U
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- holding vessel
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- cooling water
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Abstract
The utility model discloses a kind of fluid material automation storage device, it comprises: feeding engine (1) connects the discharging opening of the first and second holding vessels respectively to discharge pipe feeding, and the inlet point of the first and second holding vessels is connected by three-way valve (3), first and second holding vessels are connected feed pipe respectively by the first material inlet valve (4) with the second material inlet valve (5), first and second holding vessels all adopt jacket structured, chuck layer connects cooling mechanism, in all holding vessels, liquid level switch and temperature sensor are all installed, control circuit is according to the switch of each valve of signal control of liquid level switch and temperature sensor, the utility model precision is high, automation, in the process obviously can allocated at raw-food material, store and use, labor cost is reduced, effectively raise production efficiency, and Comparison of Management is convenient, degree of reliability is higher, is the effective measures of suitable long-run development and popularization.
Description
Technical field
The utility model relates to raw material storage device, particularly relates to the automatic storage device of a kind of food fluids raw material between multiple holding vessel.
Background technology
As everyone knows, food service industry and our life closely bound up, along with the problem of the food sanitation and safety of food service industry is in recent years more and more outstanding, this also makes food service industry automation degree of equipment more and more higher, more accurate.Traditional food service industry is to the process of the allotment of raw material, storage and use all by manually having come, and this has not only dropped into a large amount of human resources, and the wholesomeness of food and safety degree of reliability are reduced.For this reason, how the labor cost dropped into is reduced, and how to improve wholesomeness, the reliability of food, also become the topic that entire society compares concern gradually.
Improving constantly in recent years along with factory equipment degree of automation and social labor power resources costs, human resources start the equipment that is automated gradually and replace or save, but can not be fully substituted in the quite a while afterwards, a lot of enterprise is still based on labour concentrated industry now, and therefore in following a period of time, automation becomes the development tendency of society gradually.
It is not high to there is degree of automation in existing fluid material storage device, and main dependence operating personal M/C, causes production efficiency to reduce.So employing high precision, high integrated raw material automation storage device become the technical matters needing in the industry solution badly.
Utility model content
The utility model is the problems referred to above that will solve prior art, proposes the fluid material automation storage device of a kind of high precision, high integrated, high automation.
For solving the problems of the technologies described above, the technical scheme that the utility model proposes is a kind of fluid material automation storage device of design, it comprises: feeding engine, first holding vessel, second holding vessel, discharge pipe and feed pipe, the import of wherein said feeding engine connects the discharging opening of the first and second holding vessel bottoms respectively by pipeline, feeding delivery side of pump picks out pipe material, described discharge pipe connects manufacturing line materials equipment and three-way valve respectively, two outlets of this three-way valve connect the inlet point on the first and second holding vessel tops respectively, another inlet point on the first and second holding vessel tops is connected feed pipe respectively by the first material inlet valve with the second material inlet valve, described first and second holding vessels all adopt jacket structured, chuck layer connects a set of cooling mechanism for cooling fluid raw material, in first and second holding vessels, liquid level switch and temperature sensor are all installed, all liquid level switches and the equal connection control circuit of temperature sensor, control circuit is connection control three-way valve respectively, first and second material inlet valves, and the switch of each valve of signal control transmitted according to liquid level switch and temperature sensor.
Described cooling mechanism comprises a heat exchanger, the cooling water outlet of heat exchanger connects the first and second holding vessel chuck layer entrance respectively, the cooling water inlet of heat exchanger connects the first and second holding vessel chuck layer outlet respectively, the cooling water outlet or cooling water inlet of heat exchanger are connected in series circulation pump, the coolant media import of heat exchanger is connected outside refrigerating unit with coolant media outlet, and described circulation pump controls by described control circuit.
Described cooling mechanism also comprises a cooling tank, and described cooling tank is serially connected in the first holding vessel and the second holding vessel chuck layer exports between the cooling water inlet of heat exchanger.
Be connected in series the first discharge valve between the discharging opening of described first holding vessel bottom and the import of feeding engine, between the discharging opening of described second holding vessel bottom and the import of feeding engine, be connected in series the second discharge valve; First and second discharge valves control by described control circuit.
Be connected in series the first chuck valve between the cooling water outlet of described heat exchanger and the chuck layer entrance of described first holding vessel, between heat exchanger cooling water outlet and the chuck layer entrance of described second holding vessel, be connected in series the second chuck valve; First and second chuck valves control by described control circuit.
The coolant media import of described heat exchanger is connected in series a refrigerant valve, and this refrigerant valve controls by described control circuit; The cooling water outlet of described heat exchanger is connected in series a temperature sensor, and this temperature sensor connects described control circuit.
Described first holding vessel and the second holding vessel are all provided with a puddle mixer in order to stirred fluid raw material.
Compared with prior art, the utility model precision is high and automation degree of integration is high, solve the problem being entered automatic storage between different holding vessel, temperature adjustment and conveying by fluid materials such as the syrup after diluting, in the process obviously can allocated at raw-food material, store and use, labor cost is reduced, effectively raise production efficiency, and Comparison of Management is convenient, degree of reliability is higher, is the effective measures of suitable long-run development and popularization.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is described in detail, wherein:
Fig. 1 is the schematic diagram of the basic embodiment of the utility model;
Fig. 2 is the schematic diagram of the utility model preferred embodiment;
Fig. 3 is the topological diagram of the utility model electrical control part;
Fig. 4 is the control flow block diagram that the utility model realizes the conveying of fluid material automatic storage;
Fig. 5 is the control flow block diagram that the utility model realizes fluid material automatic temperature-control.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is described in further detail.Should be appreciated that specific embodiment described herein only for explaining the utility model, and be not used in restriction the utility model.
The utility model discloses a kind of fluid material automation storage device, that syrup is illustrated for fluid material below, storage device comprises: feeding engine 1, first holding vessel 21, second holding vessel 22, discharge pipe 24 and feed pipe 25, the import of wherein said feeding engine connects the discharging opening of the first and second holding vessel bottoms respectively by pipeline, feeding delivery side of pump picks out pipe material, described discharge pipe connects manufacturing line materials equipment and three-way valve 3 respectively, two outlets of this three-way valve connect the inlet point on the first and second holding vessel tops respectively, syrup is enable to be back in the first and second holding vessels, another inlet point on the first and second holding vessel tops is connected feed pipe respectively by the first material inlet valve 4 with the second material inlet valve 5, in order to be stored into by syrup in the first and second holding vessels, described first and second holding vessels all adopt jacket structured, and chuck layer connects a set of cooling mechanism for cooling fluid raw material, and syrup can cool by the cooling media in chuck layer, in first and second holding vessels, liquid level switch and temperature sensor are all installed, all liquid level switches and the equal connection control circuit of temperature sensor, control circuit is connection control three-way valve, the first and second material inlet valves the switch of each valve of signal control transmitted according to liquid level switch and temperature sensor respectively.Liquid level switch comprises and is arranged on low liquid level switch 12 on the first holding vessel sidewall and high level switch 14 in actual applications, is arranged on the low liquid level switch 13 on the second holding vessel sidewall and high level switch 15; Mounting temperature sensor 10 bottom first holding vessel, mounting temperature sensor 11 bottom the second holding vessel.
Referring to the basic embodiment shown in Fig. 1, in this example, cooling mechanism comprises a heat exchanger 28, the cooling water outlet of heat exchanger connects the entrance at the first and second holding vessel chuck layer top respectively, cooling water expansion tank under gravity, is cooled the syrup in holding vessel bottom the chuck layer by chuck layer overhead stream; The cooling water inlet of heat exchanger connects the outlet bottom the first and second holding vessel chuck layers respectively, forms turnover loop; The cooling water outlet or cooling water inlet of heat exchanger are connected in series circulation pump 2, provide circulation power to cooling water expansion tank, the coolant media import of heat exchanger is connected outside refrigerating unit with coolant media outlet, and icon 29 and 30 is the interface being connected external refrigeration unit.Described circulation pump controls by described control circuit.
Referring to the preferred embodiment shown in Fig. 2, in this example, cooling mechanism also comprises a cooling tank 23, and described cooling tank is serially connected in the first holding vessel 21 and the second holding vessel 22 chuck layer exports between the cooling water inlet of heat exchanger 28.The cooling water expansion tank of cooling tank for storing for future use.
In the preferred embodiment, between the discharging opening of described first holding vessel 21 bottom and the import of feeding engine 1, be connected in series the first discharge valve 6, between the discharging opening of described second holding vessel 22 bottom and the import of feeding engine, be connected in series the second discharge valve 7; First and second discharge valves control by described control circuit.
In the preferred embodiment, the cooling water outlet of described heat exchanger 28 is connected in series the first chuck valve 8 with between the chuck layer entrance of described first holding vessel 21, is connected in series the second chuck valve 9 between heat exchanger cooling water outlet with the chuck layer entrance of described second holding vessel 22; First and second chuck valves control by described control circuit.
In the preferred embodiment, the coolant media import of described heat exchanger 28 is connected in series a refrigerant valve 27, and this refrigerant valve controls by described control circuit; The cooling water outlet of described heat exchanger 28 is connected in series a temperature sensor 26, and this temperature sensor connects described control circuit.
In the preferred embodiment, described first holding vessel 21 and the second holding vessel 22 are all provided with a puddle mixer 31 in order to stirred fluid raw material, in order to stir the syrup in holding vessel.
Fig. 3 shows the topological diagram of electric control system, temperature sensor 10 on first holding vessel, low liquid level switch 12, temperature sensor 11 on high level switch 14 and the second holding vessel, low liquid level switch 13, the output signal of high level switch 15 and temperature sensor 26 connects this control circuit 16, and the first material inlet valve 4 of the first holding vessel, first discharge valve 6, first chuck valve 8, second material inlet valve 5 of the second holding vessel, second discharge valve 7, second chuck valve 9, threeway circulation valve 3 and refrigerant valve 27 are all connected to this control circuit, the on off state of each valve is controlled by this control circuit 16, high and low alarming value corresponding to the temperature sensor 10,11,26 of the first holding vessel, the second holding vessel and heat exchanger cooling water outlet can be set in control circuit 16, and the measured value of the temperature sensor 10,11,26 of the first holding vessel, the second holding vessel and heat exchanger cooling water outlet can be shown in real time, measure in the first holding vessel when the temperature sensor 10 of the first holding vessel specifically and judge to be greater than temperature upper limit or lowest temperature value through control circuit after material temperature, if this value of measuring is greater than temperature upper limit, control circuit can send signal makes the first chuck valve 8 open, if this value of measuring is less than lowest temperature value, control circuit can send signal makes the first chuck valve 8 close, control circuit 16 also can judge the raw material height of liquid level in the first holding vessel and the second holding vessel, and the first holding vessel and the second holding vessel rotation can be made to use, specifically when liquid level switch 12 low in the first holding vessel provides low liquid level signal, after control circuit 16 judges, provide that signal makes the first discharge valve 6 close, the second discharge valve 7 is opened, the first material inlet valve 4 is opened, threeway circulation valve 3 is opened, when in the first holding vessel, high level switch 14 provides high liquid level signal, after control circuit 16 judges, provide signal the first material inlet valve 4 is closed, when liquid level switch 13 low in the second holding vessel provides low liquid level signal, after control circuit 16 judges, provide that signal makes the second discharge valve 7 close, the first discharge valve 6 is opened, the second material inlet valve 5 is opened, threeway circulation valve 3 is closed, when in the second holding vessel, high level switch 15 provides high liquid level signal, after control circuit 16 judges, provide signal the second material inlet valve 5 is closed, in the process that circulation pump 2 runs, heat exchanger cooling water outlet temperature sensor 26 Real-Time Monitoring cooling water expansion tank leaving water temperature, when cooling water expansion tank leaving water temperature is greater than upper limit set value, control circuit can send signal makes refrigerant valve 27 open, when cooling water expansion tank leaving water temperature is less than lower limit set value, control circuit can send signal makes refrigerant valve 27 close, during enforcement, control circuit 16 is complicated control circuit, each valve can be electrically operated valve or operated pneumatic valve, and each temperature sensor, liquid level switch are monitored the holding vessel state of correspondence in real time in syrup delivery process, and accordingly the terminal valve door opening and closing state corresponding to each holding vessel is controlled.
The working process of the automatic storage temperature adjustment of fluid material described in the utility model and the control setup of conveying is illustrated below in conjunction with accompanying drawing 4 and accompanying drawing 5:
Select automatic operation mode (referring to Fig. 4), select the preferential using forestland of the first holding vessel, first holding vessel liquid level switch 12,14 is measured the two position of raw material in this tank simultaneously, and the signal of measurement is flowed to control circuit 16 in real time, namely, when the first holding vessel is not in low fluid level condition, the first holding vessel first discharge valve 6 is opened, triple valve circulation valve 3 is closed, feeding engine 1 startup optimization, if when the first holding vessel is in low fluid level condition, first holding vessel first discharge valve 6 is closed, first material inlet valve 4 is opened, feeding engine 1 is out of service, first holding vessel withdraw from use switches to the second holding vessel and uses, start toward charging in the first holding vessel after the first holding vessel first material inlet valve 4 is opened completely simultaneously, first holding vessel liquid level switch 14 is measured the high liquid level of raw material in this tank afterwards, and the signal of measurement is flowed to control circuit 16 in real time, if the first holding vessel is in high fluid level condition, the first material inlet valve 4 that then the first holding vessel is corresponding can be closed automatically, after the first holding vessel is switched to the second holding vessel, second holding vessel liquid level switch 13,15 is measured the liquid level of raw material in this tank, and the signal of measurement is flowed to control circuit 16 in real time, namely, when the second holding vessel is not in low fluid level condition, the second holding vessel second discharge valve 7 is opened, triple valve circulation valve 3 is opened, feeding engine 1 startup optimization, if when the second holding vessel is in low fluid level condition, second holding vessel second discharge valve 7 is closed, second material inlet valve 5 is opened, feeding engine 1 is out of service, second holding vessel withdraw from use switches to the first holding vessel and uses, start toward charging in the second holding vessel after the second holding vessel second material inlet valve 5 is opened completely simultaneously, second holding vessel liquid level switch 15 is measured the high liquid level of raw material in this tank afterwards, and the signal of measurement is flowed to control circuit 16 in real time, if the second holding vessel is in high fluid level condition, the second material inlet valve 5 that then the second holding vessel is corresponding can be closed automatically, if when through liquid level switch 12,14 measurement, after control circuit judges, the first holding vessel and the second holding vessel are all in low fluid level condition, first holding vessel and discharge valve 6,7 corresponding to the second holding vessel are closed, material inlet valve 4,5 is opened, first holding vessel and the charging simultaneously of the second holding vessel, switch to again and occur that the holding vessel of high liquid level uses after high liquid level appears in the first holding vessel or the second holding vessel.
Select automatic temperature-control mode of operation (referring to Fig. 5), temperature sensor 10,11 simultaneously in first, second holding vessel is measured the material temperature in first, second holding vessel respectively, the temperature value recorded is shown in real time by control circuit, and compare with the setting value in control circuit, if the measured temperature in the measured temperature in the first holding vessel or the second holding vessel is greater than the temperature upper limit of its correspondence, the first then corresponding with it holding vessel or the chuck valve open of the second holding vessel, after this valve is opened completely, circulation pump startup optimization; When the measured temperature in the measured temperature in the first holding vessel or the second holding vessel is less than the lowest temperature value of its correspondence, then the first corresponding with it holding vessel or the chuck valve closing of the second holding vessel, circulation pump is out of service; If when the temperature upper limit that the measured temperature in the measured temperature in the first holding vessel and the second holding vessel had both been not more than its correspondence is also not less than the lowest temperature value of its correspondence, then the first holding vessel and each chuck valve corresponding to the second holding vessel can not be opened, and circulation pump can not startup optimization.
More than that detailed describing is carried out to know-why of the present utility model, but protection domain of the present utility model is not only limitted to this, any known distortion that those skilled in the art do within the scope of technical conceive of the present utility model all belongs to the category involved by the utility model, as above-described embodiment gives the automatic storage temperature adjustment of the syrup source between two holding vessels and the control of conveying, but those skilled in the art apparently can be expanded to the automatic storage temperature adjustment of other raw materials between multiple holding vessel and the control of conveying, and wherein said liquid level switch also can replace with other level monitoring device well known in the art, and can be used for the overflow weir etc. of setting near holding vessel tip position, all belong to the scope of the utility model protection.
Claims (7)
1. a fluid material automation storage device, it is characterized in that comprising: feeding engine (1), first holding vessel (21), second holding vessel (22), discharge pipe (24) and feed pipe (25), the import of wherein said feeding engine connects the discharging opening of the first and second holding vessel bottoms respectively by pipeline, feeding delivery side of pump picks out pipe material, described discharge pipe connects manufacturing line materials equipment and three-way valve (3) respectively, two outlets of this three-way valve connect the inlet point on the first and second holding vessel tops respectively, another inlet point on the first and second holding vessel tops is connected feed pipe respectively by the first material inlet valve (4) with the second material inlet valve (5), described first and second holding vessels all adopt jacket structured, chuck layer connects a set of cooling mechanism for cooling fluid raw material, in first and second holding vessels, liquid level switch and temperature sensor are all installed, all liquid level switches and the equal connection control circuit of temperature sensor, control circuit is connection control three-way valve respectively, first and second input and output material valves, and the switch of each valve of signal control transmitted according to liquid level switch and temperature sensor.
2. fluid material automation storage device as claimed in claim 1, it is characterized in that: described cooling mechanism comprises a heat exchanger (28), the cooling water outlet of heat exchanger connects the first and second holding vessel chuck layer entrance respectively, the cooling water inlet of heat exchanger connects the first and second holding vessel chuck layer outlet respectively, the cooling water outlet or cooling water inlet of heat exchanger are connected in series circulation pump (2), the coolant media import of heat exchanger is connected outside refrigerating unit with coolant media outlet, and described circulation pump controls by described control circuit.
3. fluid material automation storage device as claimed in claim 2, it is characterized in that: described cooling mechanism also comprises a cooling tank (23), described cooling tank is serially connected in the first holding vessel (21) and the second holding vessel (22) chuck layer exports between the cooling water inlet of heat exchanger (28).
4. fluid material automation storage device as claimed in claim 3, it is characterized in that: between the discharging opening of described first holding vessel (21) bottom and the import of feeding engine (1), be connected in series the first discharge valve (6), between the discharging opening of described second holding vessel (22) bottom and the import of feeding engine, be connected in series the second discharge valve (7); First and second discharge valves control by described control circuit.
5. fluid material automation storage device as claimed in claim 4, it is characterized in that: be connected in series the first chuck valve (8) between the cooling water outlet of described heat exchanger (28) and the chuck layer entrance of described first holding vessel (21), between heat exchanger cooling water outlet and the chuck layer entrance of described second holding vessel (22), be connected in series the second chuck valve (9); First and second chuck valves control by described control circuit.
6. fluid material automation storage device as claimed in claim 5, is characterized in that: the coolant media import of described heat exchanger (28) is connected in series a refrigerant valve (27), and this refrigerant valve controls by described control circuit; The cooling water outlet of described heat exchanger is connected in series a temperature sensor (26), and this temperature sensor connects described control circuit.
7. the fluid material automation storage device as described in as arbitrary in claim 1 to 6, is characterized in that: described first holding vessel (21) and the second holding vessel (22) are all provided with a puddle mixer in order to stirred fluid raw material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520192227.0U CN204624370U (en) | 2015-04-01 | 2015-04-01 | Fluid material automation storage device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520192227.0U CN204624370U (en) | 2015-04-01 | 2015-04-01 | Fluid material automation storage device |
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| Publication Number | Publication Date |
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| CN204624370U true CN204624370U (en) | 2015-09-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520192227.0U Expired - Fee Related CN204624370U (en) | 2015-04-01 | 2015-04-01 | Fluid material automation storage device |
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| CN (1) | CN204624370U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106140025A (en) * | 2016-08-12 | 2016-11-23 | 嘉兴恒威电池有限公司 | Electro-hydraulic automatic reaction induction system |
| CN107096457A (en) * | 2017-06-15 | 2017-08-29 | 郑州振东科技有限公司 | Resinoid bond storage, conveying automation control system |
| CN107875961A (en) * | 2017-12-25 | 2018-04-06 | 苏州擎动动力科技有限公司 | Nano-powder decentralized system |
| CN109530019A (en) * | 2018-11-29 | 2019-03-29 | 宁夏北伏科技有限公司 | Silicon carbide micro-powder circular grinding system |
| CN112224692A (en) * | 2019-06-30 | 2021-01-15 | 西安众力沥青有限公司 | Liquid storage equipment |
-
2015
- 2015-04-01 CN CN201520192227.0U patent/CN204624370U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106140025A (en) * | 2016-08-12 | 2016-11-23 | 嘉兴恒威电池有限公司 | Electro-hydraulic automatic reaction induction system |
| CN107096457A (en) * | 2017-06-15 | 2017-08-29 | 郑州振东科技有限公司 | Resinoid bond storage, conveying automation control system |
| CN107875961A (en) * | 2017-12-25 | 2018-04-06 | 苏州擎动动力科技有限公司 | Nano-powder decentralized system |
| CN109530019A (en) * | 2018-11-29 | 2019-03-29 | 宁夏北伏科技有限公司 | Silicon carbide micro-powder circular grinding system |
| CN109530019B (en) * | 2018-11-29 | 2024-03-01 | 宁夏北伏科技有限公司 | Silicon carbide micropowder circulation grinding system |
| CN112224692A (en) * | 2019-06-30 | 2021-01-15 | 西安众力沥青有限公司 | Liquid storage equipment |
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| 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: 20150909 Termination date: 20170401 |
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| CF01 | Termination of patent right due to non-payment of annual fee |