CN203389340U - Vacuum concentration device - Google Patents
Vacuum concentration device Download PDFInfo
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- CN203389340U CN203389340U CN201320327095.9U CN201320327095U CN203389340U CN 203389340 U CN203389340 U CN 203389340U CN 201320327095 U CN201320327095 U CN 201320327095U CN 203389340 U CN203389340 U CN 203389340U
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Abstract
The utility model discloses a vacuum concentration device which comprises a concentration tank, a condensation tank and a finished product tank, and also comprises a circulating pipeline, and a Baume degree detector and a return valve which are arranged on the circulating pipeline. The concentration tank comprises an upper part and a lower part; a vaporizing tank is arranged on the upper part; a heating tank is arranged on the lower part; the vaporizing tank and the heating tank are communicated through the circulating pipeline; a raw material inlet is formed in the vaporizing tank; a hot steam inlet is formed in one side of the heating tank, and a condensate water outlet is formed in the other side of the heating tank; a steam pipeline and a discharge pipe are respectively arranged at the top and the bottom of the concentration tank; the steam pipeline is communicated with the condensation tank; the discharge pipe is communicated with the finished product tank; an emptying valve is arranged on the discharge pipe. According to the vacuum concentration device provided by the utility model, the Baume degree detector is additionally arranged, and Baume degree of honey can be detected and observed in real time, so that full-automatic production can be realized, the labor hour is saved, and the production efficiency is improved.
Description
Technical field
The utility model relates to food machinery technical field, more particularly, relates to a kind of for processing the vacuum concentrating apparatus of honey.
Background technology
The vacuum decker using in honey processing is to utilize vavuum pump to take the gas in concentration tank away, make it lower than existing ambient atmosphere air pressure, produce negative pressure, make honey material reach at a lower temperature boiling point, concentration and evaporation moisture, recycle, thereby on the basis of not destroying honey nutritional labeling, remove the moisture in honey material, sometimes the concentrating return-flow that may need repeatedly to circulate just can reach standard, in prior art, by manually at times in batches in extraction vacuum concentration pot honey material detect Baume degrees, so not only take time and effort, productivity effect is low, if Deng detecting the defective concentrated processing again again of product, can produce and more delay work the time, also influential to the quality of product.
Utility model content
The purpose of this utility model is the problem of mentioning in above-mentioned background technology in order to solve, a kind of vacuum concentrating apparatus is provided, this vacuum concentrating apparatus has installed Baume degrees detector additional, it can detect and observe the Baume degrees of honey in real time, can make to produce realization full-automatic, save man-hour, improved production efficiency.
To achieve these goals, the technical solution of the utility model is as follows:
A kind of vacuum concentrating apparatus, comprise concentration tank, drainer and finished pot, also comprise circulating line, be located at Baume degrees detector and return valve on circulating line, described concentration tank comprises, lower two parts, top is divided into evaporator, bottom is divided into heating tank, described evaporator and heating tank are communicated with by described circulating line, described evaporator is provided with feed(raw material)inlet, described heating tank one side is provided with heat steam entrance, opposite side is provided with condensation-water drain, described concentration tank top and bottom are respectively equipped with steam pipeline and discharge nozzle, described steam pipeline is communicated to described drainer, described discharge nozzle is communicated to described finished pot, on described discharge nozzle, be also provided with baiting valve.
Further, described steam pipeline two ends are respectively equipped with secondary steam entrance and secondary steam outlet, and described secondary steam entrance and secondary steam outlet are separately positioned on described drainer and described concentration tank top.
Further, described discharge nozzle is provided with self priming pump and flowmeter.Flowmeter is used for adding up the flow that enters finished pot honey material, then contrasts with the honey material in concentration tank, and it is analyzed; Self priming pump is for sucking the honey material in discharge nozzle in finished pot and store.
Further, described concentration tank top is provided with thermometer and Pressure gauge.By thermometer and Pressure gauge, temperature value and force value in can real-time monitored concentration tank, the actual conditions of being convenient to like this observe honey material in concentration tank, simple to operate, do not need manually it to be measured and is controlled, saved manpower and materials, improved efficiency.
Further, described concentration tank top is provided with and vacuumizes outlet, described in vacuumize outlet and be connected with vavuum pump.
Compared with prior art, the beneficial effects of the utility model are as follows: in the utility model, installed Baume degrees detector additional, it can detect and observe the Baume degrees of honey in real time, can effectively avoid honey material Moisture high UCL, artificial sampling in the process of concentrated processing to detect time-consuming, can make to produce and realize full-automation, improve production efficiency.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme of the utility model embodiment, below the accompanying drawing of required use during embodiment is described is briefly described, apparently, accompanying drawing in the following describes is only embodiment more of the present utility model, for those of ordinary skills, do not paying under the prerequisite of creative work, can also obtain according to these accompanying drawings other accompanying drawing.
Fig. 1 is the structural representation of the utility model vacuum concentrating apparatus;
Reference numeral: 1-concentration tank, 101-evaporator, 102-heating tank, 2-finished pot, 3-drainer, 4-steam pipeline, 5-discharge nozzle ，6-feed(raw material)inlet, 7-heat steam entrance, 8-condensation-water drain, 9-circulating line, 10-return valve, 11-Baume degrees detector, 12-baiting valve, 13-self priming pump, 14-flowmeter, 15-Pressure gauge, 16-thermometer, the outlet of 17-secondary steam, 18-secondary steam entrance, the outlet of 19-non-condensable gas, 20-condensing water inlet, 21-outlet pipe, 22-tank, 23-vacuumizes outlet.
The specific embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is only the utility model part embodiment, rather than whole embodiment.Embodiment based in the utility model, those of ordinary skills are not making the every other embodiment obtaining under creative work prerequisite, all belong to the scope of the utility model protection.
Shown in Fig. 1, a kind of vacuum concentrating apparatus, comprise concentration tank 1, drainer 3 and finished pot 2, also comprise circulating line 9, be located at Baume degrees detector 11 and return valve 10 on circulating line 9, concentration tank 1 comprises, lower two parts, top is divided into evaporator 101, bottom is divided into heating tank 102, evaporator 101 and heating tank 102 are communicated with by circulating line 9, evaporator 101 is provided with feed(raw material)inlet 6, heating tank 102 1 sides are provided with heat steam entrance 7, opposite side is provided with condensation-water drain 8, concentration tank 1 top and bottom are respectively equipped with steam pipeline 4 and discharge nozzle 5, steam pipeline 4 is communicated to drainer 3, discharge nozzle 5 is communicated to finished pot 2, on discharge nozzle 5, be also provided with baiting valve 12, steam pipeline 4 two ends are respectively equipped with secondary steam entrance 17 and secondary steam outlet 18, secondary steam entrance 17 and secondary steam outlet 18 are separately positioned on drainer 3 and concentration tank 1 top, concentration tank 1 top is provided with and vacuumizes outlet 23, vacuumize outlet 23 and be connected with vavuum pump.
Concentration tank 1 top is provided with thermometer 16 and Pressure gauge 15.By thermometer 16 and Pressure gauge 15, temperature value and force value in can real-time monitored concentration tank 1, the actual conditions of being convenient to like this observe material in concentration tank 1, simple to operate, do not need manually it to be measured and is controlled, saved manpower and materials, improved efficiency.
Concentration tank 1 has negative-pressure sealing, under the suction of vavuum pump, honey material reaches boiling point at a lower temperature, secondary steam is separated from honey material, secondary steam is drawn from the secondary steam outlet 17 at concentration tank 1 top, by steam pipeline 4, enters drainer 3, fully contacts mixing with the condensed water of the large flow flowing in drainer 3 from top to bottom, then through outlet pipe 21, flow in tank 22, non-condensable gas is discharged from non-condensable gas outlet 19.
Under suction function, honey raw material enters evaporator 101 from evaporator 101 feed(raw material)inlet 6, when honey raw material reaches a certain amount of, heat steam enters heating tank 102 from the heat steam entrance 7 of heating tank 102, to honey heating material, after boiling, form steam, meanwhile, heat steam forms the condensation-water drain 8 of condensed water from heating tank 102 and discharges after heating tank 102.
In the utility model, concentration tank 1 is connected with finished pot 2 and drainer 3, concentration tank 1 is communicated to drainer 3 by steam pipeline 4, concentration tank 1 is communicated to finished pot 2 by discharge nozzle 5, concentration tank 1 is divided into, lower two parts, top is divided into evaporator 101, bottom is divided into heating tank 102, between evaporator 101 and heating tank 102, by circulating line 9, be communicated with, circulating line 9 is provided with return valve 10 and Baume degrees tester 11, discharge nozzle 5 is provided with baiting valve 12, by this Baume degrees detector 11, can detect in real time and observe the Baume degrees of honey, when honey does not reach the Baume degrees of appointment, do not open the baiting valve 12 between concentration tank 1 and finished pot 2, do not allow honey material enter finished pot 2, open again the return valve 10 on circulating line 9, allow honey material reflux by circulating line, continue to enter and in concentration tank 1, concentrate processing, after to the last reaching standard by 11 detections of Baume degrees detector, just open the baiting valve 12 between concentration tank 1 and finished pot 2, allow honey material enter finished pot 2.
The utility model adopts steam heated and water-cooled method to process honey material, honey material in concentration tank 1 heats, realizes concentrated under vacuum state, when honey reaches after concentrated requirement, open baiting valve 12, honey material is sucked in finished pot 2 and is stored by the self priming pump 13 on discharge nozzle 5.
By increasing online visual honey Baume degrees detector 11, can effectively avoid honey material moisture superelevation in concentrated process, artificial sampling detects time-consuming, and productivity effect is low, simultaneously, if Deng detecting product defective (Moisture high UCL) concentrated processing again again, can produce the time of more delaying work, also influential to the quality of product, install Baume degrees detector 11 additional, can make to produce and carry out full-automation, improve production efficiency, save man-hour.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any modification of doing, be equal to replacement etc., within all should being included in protection domain of the present utility model.
Claims (5)
1. a vacuum concentrating apparatus, comprise concentration tank, drainer and finished pot, it is characterized in that, also comprise circulating line, be located at Baume degrees detector and return valve on circulating line, described concentration tank comprises, lower two parts, top is divided into evaporator, bottom is divided into heating tank, described evaporator and heating tank are communicated with by described circulating line, described evaporator is provided with feed(raw material)inlet, described heating tank one side is provided with heat steam entrance, opposite side is provided with condensation-water drain, described concentration tank top and bottom are respectively equipped with steam pipeline and discharge nozzle, described steam pipeline is communicated to described drainer, described discharge nozzle is communicated to described finished pot, on described discharge nozzle, be also provided with baiting valve.
2. a kind of vacuum concentrating apparatus according to claim 1, it is characterized in that, described steam pipeline two ends are respectively equipped with secondary steam entrance and secondary steam outlet, and described secondary steam entrance and secondary steam outlet are separately positioned on described drainer and described concentration tank top.
3. a kind of vacuum concentrating apparatus according to claim 1, is characterized in that, described discharge nozzle is provided with self priming pump and flowmeter.
4. a kind of vacuum concentrating apparatus according to claim 1, is characterized in that, described concentration tank top is provided with thermometer and Pressure gauge.
5. a kind of vacuum concentrating apparatus according to claim 1, is characterized in that, described concentration tank top is provided with and vacuumizes outlet, described in vacuumize outlet and be connected with vavuum pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320327095.9U CN203389340U (en) | 2013-06-06 | 2013-06-06 | Vacuum concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320327095.9U CN203389340U (en) | 2013-06-06 | 2013-06-06 | Vacuum concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203389340U true CN203389340U (en) | 2014-01-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320327095.9U Expired - Fee Related CN203389340U (en) | 2013-06-06 | 2013-06-06 | Vacuum concentration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203389340U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104587688A (en) * | 2015-01-15 | 2015-05-06 | 云南玉溪万方天然药物有限公司 | Negative pressure plant leaching solution concentration system |
| CN105533599A (en) * | 2015-12-21 | 2016-05-04 | 衡阳智源农业科技有限公司 | High efficient honey concentrator |
| CN108185393A (en) * | 2018-02-12 | 2018-06-22 | 李锦记（新会）食品有限公司 | A kind of soy sauce ammonia nitrogen value mixing system |
| CN111870976A (en) * | 2020-06-30 | 2020-11-03 | 安徽南都华铂新材料科技有限公司 | Lithium sulfate concentration device with bipolar membrane and application method thereof |
| CN113713410A (en) * | 2021-05-28 | 2021-11-30 | 阳江和鲜食品有限公司 | Honey drying method |
| TWI818557B (en) * | 2021-04-28 | 2023-10-11 | 遠東科技大學 | Room temperature type honey drying apparatus with re-dry function by pumping |
-
2013
- 2013-06-06 CN CN201320327095.9U patent/CN203389340U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104587688A (en) * | 2015-01-15 | 2015-05-06 | 云南玉溪万方天然药物有限公司 | Negative pressure plant leaching solution concentration system |
| CN105533599A (en) * | 2015-12-21 | 2016-05-04 | 衡阳智源农业科技有限公司 | High efficient honey concentrator |
| CN108185393A (en) * | 2018-02-12 | 2018-06-22 | 李锦记（新会）食品有限公司 | A kind of soy sauce ammonia nitrogen value mixing system |
| CN111870976A (en) * | 2020-06-30 | 2020-11-03 | 安徽南都华铂新材料科技有限公司 | Lithium sulfate concentration device with bipolar membrane and application method thereof |
| TWI818557B (en) * | 2021-04-28 | 2023-10-11 | 遠東科技大學 | Room temperature type honey drying apparatus with re-dry function by pumping |
| CN113713410A (en) * | 2021-05-28 | 2021-11-30 | 阳江和鲜食品有限公司 | Honey drying method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Chengguan town of Xiangfan city in 441600 Baokang County in Hubei province Paul Bay Agricultural Industrial Park Patentee after: Hubei Australia biological Polytron Technologies Inc Address before: Chengguan town of Xiangfan city in 441600 Baokang County in Hubei province Paul Bay Agricultural Industrial Park Patentee before: Hubei Aoli Biotechnology Co., Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140115 Termination date: 20180606 |
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| CF01 | Termination of patent right due to non-payment of annual fee |