CN203507564U - Equipment for evaporating and concentrating compound donkey-hide gelatin slurry extracting solution - Google Patents
Equipment for evaporating and concentrating compound donkey-hide gelatin slurry extracting solution Download PDFInfo
- Publication number
- CN203507564U CN203507564U CN201320678163.6U CN201320678163U CN203507564U CN 203507564 U CN203507564 U CN 203507564U CN 201320678163 U CN201320678163 U CN 201320678163U CN 203507564 U CN203507564 U CN 203507564U
- Authority
- CN
- China
- Prior art keywords
- pump
- compressor
- hydrops
- preheater
- complex prescription
- 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.)
- Expired - Lifetime
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- 238000001704 evaporation Methods 0.000 title claims abstract description 24
- 108010010803 Gelatin Proteins 0.000 title abstract 4
- 150000001875 compounds Chemical class 0.000 title abstract 4
- 229920000159 gelatin Polymers 0.000 title abstract 4
- 239000008273 gelatin Substances 0.000 title abstract 4
- 235000019322 gelatine Nutrition 0.000 title abstract 4
- 235000011852 gelatine desserts Nutrition 0.000 title abstract 4
- 239000002002 slurry Substances 0.000 title abstract 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 229920000715 Mucilage Polymers 0.000 claims description 26
- 239000000853 adhesive Substances 0.000 claims description 26
- 239000003292 glue Substances 0.000 claims description 26
- 241000521257 Hydrops Species 0.000 claims description 24
- 206010030113 Oedema Diseases 0.000 claims description 24
- 230000008020 evaporation Effects 0.000 claims description 21
- 238000007599 discharging Methods 0.000 claims description 12
- 239000012530 fluid Substances 0.000 claims description 11
- 238000000926 separation method Methods 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 6
- 239000012141 concentrate Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000008234 soft water Substances 0.000 claims description 3
- 230000006835 compression Effects 0.000 description 6
- 238000007906 compression Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009194 climbing Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 241000411851 herbal medicine Species 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Images
Abstract
The utility model provides equipment for evaporating and concentrating compound donkey-hide gelatin slurry extracting solution. The equipment at least comprises a raw liquid tank, an accumulated liquid tank, a condensate tank, an evaporator, a vacuum pump water tank, a preheater, a separator, a feed pump, an accumulated liquid pump, a condensate pump, a discharge pump, a vacuum pump, a first compressor and a second compressor, wherein the raw liquid tank, the feed pump and the preheater are sequentially connected through pipelines so as to form a preheating system, the raw liquid tank is used for storing the compound donkey-hide gelatin slurry to be treated, and the feed pump is used for conveying the compound donkey-hide gelatin slurry to the preheater for preheating. The equipment has the advantages of energy saving, environment friendliness, low operation cost, small area occupation and high automation degree.
Description
Technical field
The utility model relates to a kind of evaporation concentration equipment of complex prescription glue mucilage extract.
Background technology
The evaporation concentration technique of Chinese herbal medicine industry generally adopts traditional single-action, economic benefits and social benefits and triple effect Steam Heating concentration technique at present.On traditional evaporation and concentration basis, developed again afterwards heat pump techniques and inscribe circulating technology, heat pump and inscribe circulating technology also start to be widely used at Chinese pharmaceutical industry; Within 2010, by market, recognize, the vacuum compression concentration technique for chemical industry enters China at home, and brings into use in the industries such as chemical industry, wastewater treatment.
Mechanical steam recompression (MVR) evaporimeter, its principle is the indirect steam that utilizes high energy efficiency vapour compression machine Compression Evaporation to produce, electric energy energy transform into heat energy, improve the enthalpy of indirect steam, the indirect steam that is enhanced heat energy is squeezed into vaporization chamber and is heated, to reach, recycle the existing heat energy of indirect steam, thereby can not need outside fresh steam, by evaporimeter self-loopa, realize the object of evaporation and concentration.By forms such as PLC, industrial computer (FA), configurations, come control system temperature, pressure, motor rotary speed, keeping system evaporation balance.Theoretically, use MVR evaporimeter to save more than 80% energy than conventional evaporator, save more than 90% condensed water, reduce more than 50% floor space.
Utility model content
The technical problem that the utility model solves is, a kind of energy-conserving and environment-protective are provided, and operating cost is low, and floor space is little, the complex prescription glue mucilage evaporation concentration equipment that automaticity is high.
In order to address the above problem, the utility model provides a kind of evaporation concentration equipment of complex prescription glue mucilage extract, at least comprise original fluid container, hydrops tank, solidifying water pot, vavuum pump water pot, evaporimeter, preheater, separator, feed pump, hydrops pump, condensate pump, discharging pump, vavuum pump, the first compressor, the second compressor, described original fluid container, feed pump, preheater connect successively by pipeline, form pre-heating system; Described original fluid container is for storing pending complex prescription glue mucilage; Described feed pump carries out preheating for complex prescription glue mucilage is transported to described preheater to complex prescription glue mucilage.
Further, described evaporimeter, separator, discharging pump, the first compressor, the second compressor, vavuum pump, vavuum pump water pot connect successively by pipeline, form vapo(u)rization system; Described evaporimeter passes into fresh steam for complex prescription glue mucilage is carried out to evaporation and concentration; Fresh steam enters described separator to carrying out gas-liquid separation, and the concentrate after separation enters separator bottom and discharges by described discharging pump, and steam up enters the first compressor, the second compressor compresses is transmitted back to described evaporimeter again.
Further, described solidifying water pot, condensate pump, hydrops tank, hydrops pump connect successively by pipeline, form condensate system; Described hydrops tank is for collecting the condensed water of described the first compressor and being transported to described solidifying water pot by described hydrops pump; Described solidifying water pot is for collecting the condensed water of described evaporimeter, hydrops tank and being transported to described preheater by described condensate pump.
Further, the condensed water that described vavuum pump water pot is discharged is input to respectively described feed pump, hydrops pump, condensate pump, discharging pump, vavuum pump, carries out cooling.
Further, described the second compressor is undertaken cooling by soft water.
The utility model has the advantages that:
Energy-conserving and environment-protective, operating cost is low, and floor space is little, and automaticity is high.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
The specific embodiment
Hereinafter in connection with accompanying drawing, embodiment of the present utility model is elaborated.It should be noted that, in the situation that not conflicting, embodiment and the feature in embodiment in the application can be combined mutually.
The utility model provides the evaporation concentration equipment of a kind of complex prescription glue mucilage extract as shown in Figure 1, at least comprise original fluid container 1, hydrops tank 2, solidifying water pot 3, vavuum pump water pot 4, evaporimeter 5, preheater 6, separator 7, feed pump 8, hydrops pump 9, condensate pump 10, discharging pump 11, vavuum pump 12, the first compressor 13, the second compressor 14, original fluid container 1, feed pump 8, preheater 6 connect successively by pipeline, form pre-heating system; Original fluid container 1 is for storing pending complex prescription glue mucilage; Feed pump 8 carries out preheating for complex prescription glue mucilage being transported to 6 pairs of complex prescription glue mucilages of preheater.
Evaporimeter 5, separator 7, discharging pump 11, the first compressor 13, the second compressor 14, vavuum pump, vavuum pump water pot 4 connect successively by pipeline, form vapo(u)rization system; Evaporimeter 5 passes into fresh steam for complex prescription glue mucilage is carried out to evaporation and concentration; Fresh steam enters 7 pairs of separators and carries out gas-liquid separation, and the concentrate after separation enters separator 7 bottoms and discharges by discharging pump 11, and steam up enters the first compressor 13, the second compressor 14 compressions are transmitted back to evaporimeter 5 again; Vavuum pump 12, for the air in system is extracted out, forms vacuum.
Solidifying water pot 3, condensate pump 10, hydrops tank 2, hydrops pump 9 connect successively by pipeline, form condensate system; Hydrops tank 2 is for collecting the condensed water of the first compressor 13 and being transported to solidifying water pot 3 by hydrops pump 9; Solidifying water pot 3 is for collecting the condensed water of evaporimeter 5, hydrops tank 2 and being transported to preheater 6 by condensate pump 10.
The condensed water that vavuum pump water pot 4 is discharged is input to respectively feed pump 8, hydrops pump 9, condensate pump 10, discharging pump 11, vavuum pump 12, carries out cooling.
The second compressor 14 is undertaken cooling by soft water.
Equipment workflow:
1. charging: pending complex prescription glue mucilage is stored in original fluid container 1, squeezes into vapo(u)rization system by feed pump 8.
Complex prescription glue mucilage from original fluid container 1 out, is squeezed into preheater (plate type heat exchanger) 6 by feed pump 8, complex prescription glue mucilage and preheater 6 heat exchange.Complex prescription glue mucilage stoste, through preheating, reaches after 95 ℃, enters evaporimeter 5 and carries out evaporation and concentration.
2. while evaporating, the feeding liquid of 8000kg/h carries out evaporation and concentration in integral type two effect climbing film evaporators 5, thereafter in separator 7, carry out gas-liquid separation, the concentrate after separation enters separator 7 bottoms, and steam up enters compressor compresses after baffle plate is removed liquid.
3. the steam after compressor increasing temperature and pressure comes back to the shell side of evaporimeter 5, and after material-heat-exchanging in tube side, is condensed into water and discharges system, the material evaporation in tube side or intensification.
4. concentrate reaches after desired solid-to-liquid ratio, through on-line densimeter, measures, and carries out discharging after reaching desired density.
5. from out 95 ℃ of separator 7, the indirect steam of 3000kg/h, enters MVR compressibility.After indirect steam is compressed, temperature can be elevated to 105 ℃ of left and right, and the steam after compression is squeezed into evaporimeter 5 again and added thermal material.Add in the process of thermal material, this part steam-condensation becomes water and is discharged by condensate pump 10, and its temperature is about 105 ℃.
6. the material after preheating enters after evaporimeter 5, and after compression, is elevated to the indirect steam of 105 ℃ and carries out heat exchange, and whole system reaches thermal balance, and now the shaft power of compressor is 37*2kw.
Company is now with triple effect energy consumption testing and the contrast of MVR technical testing
1, now use triple effect technical testing
2, company now uses three effect techniques and MVR technology energy consumption comparison
3, every annual operating and maintenance cost contrast table of two kinds of technology
The foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, for a person skilled in the art, the utility model can have various modifications and variations.All within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (5)
1. the evaporation concentration equipment of a complex prescription glue mucilage extract, at least comprise original fluid container, hydrops tank, solidifying water pot, vavuum pump water pot, evaporimeter, preheater, separator, feed pump, hydrops pump, condensate pump, discharging pump, vavuum pump, the first compressor, the second compressor, it is characterized in that:
Described original fluid container, feed pump, preheater connect successively by pipeline, form pre-heating system;
Described original fluid container is for storing pending complex prescription glue mucilage; Described feed pump carries out preheating for complex prescription glue mucilage is transported to described preheater to complex prescription glue mucilage.
2. the evaporation concentration equipment of a kind of complex prescription glue mucilage extract as claimed in claim 1, is characterized in that:
Described evaporimeter, separator, discharging pump, the first compressor, the second compressor, vavuum pump, vavuum pump water pot connect successively by pipeline, form vapo(u)rization system;
Described evaporimeter passes into fresh steam for the extract of complex prescription glue mucilage is carried out to evaporation and concentration; Fresh steam enters described separator extract is carried out to gas-liquid separation, and the concentrate after separation enters separator bottom and discharges by described vavuum pump, and steam successively enters the first compressor, the second compressor compresses is transmitted back to described evaporimeter again.
3. the evaporation concentration equipment of a kind of complex prescription glue mucilage extract as claimed in claim 2, is characterized in that:
Described solidifying water pot, condensate pump, hydrops tank, hydrops pump connect successively by pipeline, form condensate system; Described hydrops tank is for collecting the condensed water of described the first compressor and being transported to described solidifying water pot by described hydrops pump; Described solidifying water pot is for collecting the condensed water of described evaporimeter, hydrops tank and being transported to described preheater by described condensate pump.
4. the evaporation concentration equipment of a kind of complex prescription glue mucilage extract as claimed in claim 3, is characterized in that:
The condensed water that described vavuum pump water pot is discharged is input to respectively described feed pump, hydrops pump, condensate pump, discharging pump, vavuum pump, carries out cooling.
5. the evaporation concentration equipment of a kind of complex prescription glue mucilage extract as claimed in claim 4, is characterized in that:
Described the second compressor is undertaken cooling by soft water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320678163.6U CN203507564U (en) | 2013-10-30 | 2013-10-30 | Equipment for evaporating and concentrating compound donkey-hide gelatin slurry extracting solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320678163.6U CN203507564U (en) | 2013-10-30 | 2013-10-30 | Equipment for evaporating and concentrating compound donkey-hide gelatin slurry extracting solution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203507564U true CN203507564U (en) | 2014-04-02 |
Family
ID=50366549
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320678163.6U Expired - Lifetime CN203507564U (en) | 2013-10-30 | 2013-10-30 | Equipment for evaporating and concentrating compound donkey-hide gelatin slurry extracting solution |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203507564U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104524798A (en) * | 2015-01-18 | 2015-04-22 | 丁武轩 | Continuous evaporation and crystallization device and method capable of saving energy by mechanical steam recompression |
| CN104771921A (en) * | 2015-04-14 | 2015-07-15 | 徐翔 | Atmospheric synergetic MVR energy saving unit and energy saving process |
| CN106036514A (en) * | 2016-05-30 | 2016-10-26 | 江苏哈工药机科技股份有限公司 | Colla corii asini melting technology for production of colla corii asini cakes |
| CN107137947A (en) * | 2017-06-12 | 2017-09-08 | 山东东阿国胶堂阿胶药业有限公司 | Donkey-hide gelatin production evaporator and seperator steam water circulation utilization system |
-
2013
- 2013-10-30 CN CN201320678163.6U patent/CN203507564U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104524798A (en) * | 2015-01-18 | 2015-04-22 | 丁武轩 | Continuous evaporation and crystallization device and method capable of saving energy by mechanical steam recompression |
| CN104524798B (en) * | 2015-01-18 | 2016-06-08 | 丁武轩 | The continuous evaporative crystallization device of function of mechanical steam recompression and continuous evaporative crystallization method |
| CN104771921A (en) * | 2015-04-14 | 2015-07-15 | 徐翔 | Atmospheric synergetic MVR energy saving unit and energy saving process |
| CN106036514A (en) * | 2016-05-30 | 2016-10-26 | 江苏哈工药机科技股份有限公司 | Colla corii asini melting technology for production of colla corii asini cakes |
| CN106036514B (en) * | 2016-05-30 | 2020-07-17 | 江苏哈工药机科技股份有限公司 | Gelatin melting process for production of donkey-hide gelatin cakes |
| CN107137947A (en) * | 2017-06-12 | 2017-09-08 | 山东东阿国胶堂阿胶药业有限公司 | Donkey-hide gelatin production evaporator and seperator steam water circulation utilization system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140402 |
|
| CX01 | Expiry of patent term |