CN205088156U - Can improve natural borneol extraction system who receives yield - Google Patents
Can improve natural borneol extraction system who receives yield Download PDFInfo
- Publication number
- CN205088156U CN205088156U CN201520893292.6U CN201520893292U CN205088156U CN 205088156 U CN205088156 U CN 205088156U CN 201520893292 U CN201520893292 U CN 201520893292U CN 205088156 U CN205088156 U CN 205088156U
- Authority
- CN
- China
- Prior art keywords
- water
- condensation
- steam
- communicated
- natural broneolum
- 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.)
- Active
Links
Landscapes
- Medicines Containing Plant Substances (AREA)
Abstract
The utility model provides a can improve natural borneol extraction system who receives yield to solve current extraction system and receive the technical problem that the yield is low, it include the boiling bulb that is equipped with the steam distributor in its bottom and with the steam outlet of boiling bulb corresponds the condenser of intercommunication, and the steam inlet of the steam distributor in this boiling bulb passes through the saturated steam pipeline and corresponds the intercommunication with the saturated steam generating set, it includes still that one is used for the condensate recovery's after the condenser condensation the comdenstion water bucket of keeping in, the comdenstion water keep in the bucket through the water pump still with the inside intercommunication of boiling bulb is in order to pass through the water pump is kept in the comdenstion water collected in the bucket with the comdenstion water and is carried to the boiling bulb in. Through this system and method for, do not need again to reform transform current cooling system in implementation, also need not be to the transformation of automizing of steam flow control system and control method, practiced thrift the transformation expense of enterprise.
Description
Technical field
The utility model relates to natural Broneolum Syntheticum extractive technique field, particularly relates to a kind of natural Broneolum Syntheticum extraction system improving recovery rate.
Background technology
Natural Broneolum Syntheticum is as a kind of Chinese medicine, and it is white crystalline powder or plate crystal body, gas delicate fragrance, and taste is pungent, cool, be the fresh branch of canella borneol camphor tree, leaf through extract be processed into; It is mainly distributed in south and southwestern each provinces and regions, has inducing resuscitation of having one's ideas straightened out, effect of clearing away heat to and alleviating pain, is usually used in pyreticosis coma, faints from fear, apoplexy coma due to blocking of the respiratory system, and the obstruction of the circulation of vital energy is fainted cruelly, and middle evil stupor, Obstruction of qi in the chest and cardialgia, hot eyes, aphtha, swelling and pain in the throat, duct is suppurated.Ji'an City woods section of the eighties in last century Jiangxi Province find in the branches and leaves of borneol camphor tree containing 0.5% ~ 3% natural Broneolum Syntheticum and borneol oil, and propose method natural Broneolum Syntheticum and borneol oil extracted from borneol camphor tree branches and leaves, the extracting method of this natural Broneolum Syntheticum and borneol oil mainly at ambient pressure, adopts the method for steam distillation.Be specially:
1, the borneol camphor tree branches and leaves of felling are mated formation uniformly in air distillation pot, build pot cover, and still pot and condenser are communicated as one.
2, logical water quench in condenser chuck.
3, the steam in boiler passes into the bottom of still pot, distills borneol camphor tree branches and leaves.
In aforesaid operations, it (is controlled by the exhaust gas conditions of venting port on observation natural Broneolum Syntheticum and borneol oil gathering barrel and the condensate flow of condensation-water drain by Artificial Control vapor pressure (standard is that still pot water seal does not leak vapour, water seal height 20 centimetres) and steam flow.Adopt the size of the vapor pressure on regulating and controlling valve steam-pipe below to control flow, the experience completely with control vapour personnel controls.Through actual mensuration, steam flow control 120 ~ 200 ㎏/hour scope in).After draining the air in water distilling apparatus, distillation time keeps 1 hour, and distillation terminates.In whole still-process, steam regulation control valve at any time, in the scope vapor pressure in still pot and steam flow being remained on oneself consider appropriate.
4, after distillation terminates, the borneol camphor tree branches and leaves in still pot are taken out, reloads new borneol camphor tree branches and leaves, carry out the distillation of next pot.
5, when after continuous still battery 4 ~ 8 pots, open condenser cover, with scoop by under the natural ice slice bar that condenses on condenser inner wall, allow it fall into natural Broneolum Syntheticum gathering barrel, with strainer, the natural Broneolum Syntheticum in gathering barrel and borneol oil are pulled out.This production batch terminates, and then continues the production of next batch.
6, it is centrifugal that whizzer put into by the natural Broneolum Syntheticum pulled out and borneol oil, by natural Broneolum Syntheticum with borneol is separating of oil comes.They carry out processing treatment by entering into rear operation separately.
And found by aforesaid operations, when extracting the borneol camphor tree branches and leaves of same weight, adopt its ultimate production of existing system little, the recovery rate of every kilogram of borneol camphor tree branches and leaves extraction natural Broneolum Syntheticum is low, and human factor is very large on the impact of natural Broneolum Syntheticum recovery rate in its production operation, meanwhile, the water of condensation after condenser condenses is directly drained as waste water, causes the problem of environmental pollution.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, adapt to reality need, a kind of natural Broneolum Syntheticum extraction system improving recovery rate is provided, current existing extraction system recovery rate is low, output is little to solve, human factor impact is large, the technical problem of contaminate environment.
In order to realize the purpose of this utility model, the technical scheme that the utility model adopts is:
Design a kind of natural Broneolum Syntheticum extraction system improving recovery rate, it comprises in bottom it the still pot and the condenser that be communicated with corresponding to the vapour outlet of described still pot that are provided with steam distributor, and the steam distributor steam inlet in this still pot is communicated with by saturated vapor pipeline is corresponding with saturated vapor producer; It also comprises a water of condensation temporary storage barrel for being carried out reclaiming by the water of condensation after condenser condenses; Described water of condensation temporary storage barrel is also communicated with the inside of described still pot by water pump, to be delivered in still pot by the water of condensation collected in water of condensation temporary storage barrel by described water pump.
Further, also comprise the product-collecting bucket which is provided with bung, the outlet of described condenser and the inlet communication of this product-collecting bucket; One is also provided with for the water outlet by the water of condensation discharge in this product-collecting bucket at the middle part of described product-collecting bucket, and a vertically disposed pipeline is provided with in this product-collecting bucket, the upper end of this pipeline is communicated with described water outlet, at the bottom of the lower end of this pipeline is arranged at barrel; Be communicated with via a drainage element is corresponding with described water of condensation temporary storage barrel with the water outlet that described pipeline upper end is communicated with; Described drainage element is without blocking diversion trench; Describedly comprise without blocking diversion trench the lower U-lag main body and upper U-lag groove lid that its section all takes the shape of the letter U, described upper U-lag groove cover buckle in described lower U-lag main body, so that the passage formed between the two is formed condensation flow circulation passage.
Further, water of condensation import is also offered in the bottom of described still pot; Described water of condensation temporary storage barrel is communicated with by water pump is corresponding with described water of condensation import.
Further, described saturated vapor pipeline is also corresponding with described water of condensation import to be communicated with, and pipeline between described saturated vapor pipeline and described water of condensation import is also provided with the second steam control valve.
Further, the saturated vapor pipeline that the steam distributor in described still pot is communicated with steam generating stove is also provided with the first steam control valve.
Further, the inwall of described still pot middle and lower part is also provided with the first pressure tap, this first pressure tap is communicated with by the first pressure measurement control valve is corresponding with minute-pressure measuring cell.
Further, the saturated vapor pipeline of described first steam control valve steam output end offers the second pressure tap, this second pressure tap is communicated with by the second pressure measurement control valve is also corresponding with described minute-pressure measuring cell.
Further, the saturated vapor pipeline of described first steam control valve admission end is also provided with tensimeter.
Further, described minute-pressure measuring cell comprise in it fill liquid and the transparent tube arranged that takes the shape of the letter U, and by retaining plate fixing for described transparent tube; And also scale marks is provided with along in the vertical direction of described transparent tube on described retaining plate; One end of described transparent tube is communicated with described first pressure measurement control valve is corresponding with the second pressure measurement control valve by tee pipe fitting, its other end opening.
Further, the water of condensation ingress bottom described still pot is also provided with the liquid discharge pipe of being discharged by the liquid in this still pot, and is also provided with discharge opeing control valve on this liquid discharge pipe.
Further, by the method for native system extraction natural Broneolum Syntheticum be:
Borneol camphor tree branches and leaves are put into still pot and are distilled by the first step, and the steam that distillation produces enters condensation in condenser, collect the water of condensation produced through condenser;
Second step, carries out distillation process, to be separated out with steam by the natural Broneolum Syntheticum in water of condensation by the water of condensation of collection;
3rd step: the steam distilling generation in second step is entered condensation in condenser.
Further, concrete is, above-mentionedly states in the first step, and the water of condensation that condenser produces enters in water of condensation temporary storage barrel and collects;
In the described the first step, water of condensation is entered after collecting in water of condensation temporary storage barrel, also comprise the borneol camphor tree branches and leaves after by distillation in still pot and take out, by the step that the liquid in still pot is discharged;
Described second step is specially: in still pot, put into new borneol camphor tree branches and leaves, is sent in still pot by the water of condensation in water of condensation temporary storage barrel by water pump, continues to carry out distillation process to the water of condensation in still pot and the new borneol camphor tree branches and leaves loaded;
Described 3rd step is specially: enter condensation in condenser by second step heating up in a steamer in pot the steam distilling generation.
Also comprise the 4th step: the first step, second step, the 3rd step described in repetitive operation;
5th step: the borneol camphor tree branches and leaves after distillation in still pot are taken out, and the liquid in still pot is discharged; The natural Broneolum Syntheticum that condenser inner wall is formed is collected simultaneously.
Further, being sent into after in still pot by the water of condensation in water of condensation temporary storage barrel by water pump, described second steam control valve is opened, and now, steam enters in described still pot via water of condensation import.
The beneficial effects of the utility model are:
1. the utility model carries out distillation process by being sent in still pot by the original water of condensation as waste water, reclaims natural Broneolum Syntheticum wherein, and then can improve recovery rate (extraction yield) and the productivity effect of natural Broneolum Syntheticum.
2. nothing blocking diversion trench of the present utility model in use avoids natural Broneolum Syntheticum to condense in generation conveying pipeline inner wall causing line clogging phenomenon, to ensure the normal operation of this system.
3. the utility model also has other beneficial effects, will propose in the lump in an embodiment.
Accompanying drawing explanation
Fig. 1 is the primary structure schematic diagram of native system;
Fig. 2 is the nothing blocking diversion trench primary structure schematic diagram in native system;
Fig. 3 is the minute-pressure measuring cell primary structure schematic diagram in native system;
In figure: 1. saturated vapor producer; 2. tensimeter; 3. saturated vapor pipeline; 4. tee pipe fitting; 5. the first steam control valve; 6. the second pressure measurement control valve; 7. the first pressure measurement control valve; 8. minute-pressure measuring cell; 9. the first pressure tap; 10. the second pressure tap; 11. second steam control valves; 12. water of condensation imports; 13. still pots; 14. water pumps; 15. water of condensation temporary storage barrels; 16. without blocking diversion trench; 17. condensers; Pipeline between 18. still pots and condenser; 19. cover plates; 20.U shape groove body; 21. transparent tube; 22. retaining plates; 23. scale markss; 24. discharge opeing control valves; 25. liquid discharge pipes; 26. product-collecting buckets; 27. pipelines.
Embodiment
Below in conjunction with drawings and Examples, the utility model is further illustrated:
The present inventor is finding that existing system and method mainly exists following problem through long-term production practice with repeatedly in experimental demonstration:
In the prior art, water of condensation is used as waste water to drain, and due to natural Broneolum Syntheticum and the oily smell that there is uniqueness of borneol, and its smell is very heavy, it will cause certain pollution to Working environment after discharging; And contriver finds that in long-term production practice the water vapor that water of condensation is separated out condensation can have crystal after repeatedly contacting with wall on wall, meanwhile, the pipeline of discharge water of condensation also often can be blocked; Tamper in the crystal that wall condenses and pipeline takes out rear for this reason and analyzes it by contriver; Contriver is finding that after long-term analysis this crystal is natural Broneolum Syntheticum unexpectedly, this discovery very shocks the present inventor, because before this, the expert in this area unanimously thinks in water of condensation it is not containing natural Broneolum Syntheticum, even if or be also micro-containing it; For this reason, the present inventor, by being further analyzed discovery to water of condensation, is not do not have natural Broneolum Syntheticum in its water of condensation, but containing a large amount of natural Broneolum Syntheticums, therefore, wall just has the crystal of condensation.Therefore, in prior art, water of condensation is used as waste water and drains very unfortunate, also result in serious waste, also make the recovery rate of existing system low simultaneously.
For this reason, contriver is by finding after the water of condensation reclaimed in the lab experimental analysis: when water temperature is 53 DEG C, natural Broneolum Syntheticum recovery rate 0.126% in water of condensation; When water temperature is 55 DEG C, natural Broneolum Syntheticum recovery rate 0.128% in water of condensation; When water temperature is 58 DEG C, natural Broneolum Syntheticum recovery rate 0.130% in water of condensation; When water temperature is 65 DEG C, natural Broneolum Syntheticum recovery rate 0.135% in water of condensation.This illustrates: 1. water temperature is higher, and the natural Broneolum Syntheticum be dissolved in water is more.2. condensation water quantity is more, and water temperature is higher, its distill time waste natural Broneolum Syntheticum more, therefore in water of condensation natural Broneolum Syntheticum more.And say in this way in about the document of natural Broneolum Syntheticum: natural Broneolum Syntheticum is slightly soluble in water.Find by analyzing, above-mentioned conclusion more should refer to that natural Broneolum Syntheticum is slightly soluble in cold water, and practical situation should be: natural ice sector-meeting is dissolved in water, and the higher meltage of water temperature is more.When adopting the method for wet distillation to extract natural Broneolum Syntheticum, the inevitable temperature higher than water coolant of temperature of water of condensation, condenser cooling performance is poorer, then the temperature of water of condensation is higher than the temperature of water coolant must be more.In actual production process, must contain natural Broneolum Syntheticum in the water of condensation after distillation, and condensate temperature is higher, natural Broneolum Syntheticum amount is wherein more.
Contriver is analyzing above and can drawing to draw a conclusion after test: under the prerequisite that the natural Broneolum Syntheticum in borneol camphor tree branches and leaves and borneol oil all distill, how many decision natural Broneolum Syntheticums of amount of natural Broneolum Syntheticum run off with water of condensation and the size of the recovery rate of borneol oil; Therefore in reduction water of condensation natural Broneolum Syntheticum content (namely reducing the temperature of water of condensation) or carry out reclaiming to the natural Broneolum Syntheticum in water of condensation and can improve production efficiency and the product recovery rate of enterprise significantly; If but the condensing equipment purchasing new good cooling results is specially to reduce the temperature of water of condensation, reach the object reducing natural Broneolum Syntheticum loss, then the input of enterprise is too large, thoroughly can not solve natural Broneolum Syntheticum and run off and the problem of loss with water of condensation.Therefore, contriver transforms existing steam distillation apparatus, when making full use of its existing apparatus and equipment, a set of condensate water recovery device is added with a small amount of investment, natural Broneolum Syntheticum in water of condensation is reclaimed completely, reach and farthest improve output, the object reduced costs.
Current inventor provides a kind of natural Broneolum Syntheticum extraction system improving recovery rate for this reason; It is realized by following examples:
Embodiment 1: a kind of natural Broneolum Syntheticum extraction system improving recovery rate, see Fig. 1 to Fig. 3; It comprises in bottom it the still pot 13 and the condenser 17 that be communicated with corresponding to the vapour outlet of described still pot 13 that are provided with steam distributor, and the vapour outlet of this condenser 17 and still pot 13 is communicated with by the pipeline 18 between still pot and condenser; Meanwhile, the steam distributor steam inlet in this still pot 13 is communicated with by saturated vapor pipeline 3 is corresponding with the vapour outlet of saturated vapor producer 1; Further, native system key Design part it also comprise one for the water of condensation temporary storage barrel 15 by condensed for condenser 17 condensing hot air furnace.
It also comprises the product-collecting bucket 26 which is provided with bung, and the outlet of described condenser 17 is directly communicated with this product-collecting bucket 26 import; One is also provided with for the water outlet by the water of condensation discharge in this product-collecting bucket at the middle part of described product-collecting bucket 26, and in this product-collecting bucket 26, be provided with a vertically disposed pipeline 27, the upper end of this pipeline 27 is communicated with described water outlet, at the bottom of the lower end of this pipeline is arranged at barrel; Be communicated with via a drainage element is corresponding with described water of condensation temporary storage barrel 15 with the water outlet that described pipeline upper end is communicated with; And above-described drainage element is without blocking diversion trench 16; This nothing blocking diversion trench it comprise the lower U-lag main body 20 and upper U-lag groove lid 19 that its section all takes the shape of the letter U, described upper U-lag groove lid 19 is buckled in described lower U-lag main body 20, so that the passage formed between the two is formed condensation flow circulation passage.The generation of the crystal blocking condensation flow circulation passage phenomenon that this nothing blocking diversion trench 16 in use can avoid water of condensation to separate out, simultaneously, even if crystallize out on the inwall without blocking diversion trench 16, after only upper U-lag groove lid 19 need being taken out, removed, simultaneously from the part without the crystal removed in blocking diversion trench 16 being also product.
In the application, the steam containing natural Broneolum Syntheticum and borneol oil steamed through still pot enters condensation in condenser, in the process, its most of natural Broneolum Syntheticum condenses on the inwall of condenser, and its borneol oil flows in product-collecting bucket with the crystal of part natural Broneolum Syntheticum with the water of condensation containing natural Broneolum Syntheticum; Flow into the difference of water of condensation, natural Broneolum Syntheticum and the borneol oil in product-collecting bucket 26 due to density, the density of its natural Broneolum Syntheticum, borneol oil is little and be positioned at the top of water of condensation, and condensed water level is in the below of natural Broneolum Syntheticum and borneol oil, therefore by the product-collecting bucket of the design, its water of condensation can be expelled in water of condensation temporary storage barrel 15 by pipeline 27 from the bottom of product-collecting bucket and store, and the natural Broneolum Syntheticum on the water of condensation water surface, borneol oil can not be discharged product-collecting bucket again.
The described water of condensation temporary storage barrel 15 of the design is also communicated with described still pot 13 inside by water pump 14, to be delivered in still pot 13 by described water pump 14 by the water of condensation collected in water of condensation temporary storage barrel 15; Concrete, offer water of condensation import 12 in the bottom of described still pot 13; Described water of condensation temporary storage barrel 15 is communicated with by water pump 14 is corresponding with described water of condensation import 12.Simultaneously, water of condensation ingress 12 bottom described still pot is also provided with the liquid discharge pipe 25 of being discharged by the liquid in this still pot, and discharge opeing control valve 24 is also provided with on this liquid discharge pipe, this liquid discharge pipe 25 forms blow-off pipe, to be discharged by the waste water in still pot by this liquid discharge pipe 25.
Further, described saturated vapor pipeline 3 is communicated with by tee pipe fitting is also corresponding with described water of condensation import 12, and pipeline between described saturated vapor pipeline 3 and described water of condensation import 12 is also provided with the second steam control valve 11.The saturated vapor pipeline 3 that still pot 13 is communicated with steam generating stove 1 is also provided with the first steam control valve 5.The saturated vapor pipeline 3 of described first steam control valve 5 admission end is also provided with tensimeter 2.
And in order to the pressure change that controls and observe in still pot and scope, the design is also also provided with the first pressure tap 9 on the inwall of still pot 13 middle and lower part, this first pressure tap 9 is communicated with by the first pressure measurement control valve 7 is corresponding with minute-pressure measuring cell 8.The saturated vapor pipeline 3 of described first steam control valve 5 steam output end offers the second pressure tap 10, and this second pressure tap 10 is communicated with by the second pressure measurement control valve 6 is also corresponding with described minute-pressure measuring cell 8.Further, the design's minute-pressure measuring cell 8 used it comprise in it fill liquid and the transparent tube 21 arranged that takes the shape of the letter U, and by retaining plate 22 fixing for described transparent tube 21; And scale marks 23 is also provided with along in the vertical direction of described transparent tube on described retaining plate 22; One end of described transparent tube 21 is also communicated with described first pressure measurement control valve is corresponding with the second pressure measurement control valve by tee pipe fitting, and its other end opening is arranged.The pressure size in saturated vapor pipeline 3 and still pot 13 in use can be monitored by the open and close of control first pressure measurement control valve and the second pressure measurement control valve, and then the pressure size controlled in still pot 13 and enter the steam flow of still pot 13.
Further, as follows by the method for native system extraction natural Broneolum Syntheticum:
The first step, borneol camphor tree branches and leaves are put into still pot distill, the steam that distillation produces enters into condenser condensation with natural Broneolum Syntheticum and borneol oil, in this process, natural Broneolum Syntheticum major part condenses on condenser inner wall, small part enters in product-collecting bucket, simultaneously, vapor condensation becomes water of condensation, the borneol oil cooling liquid that congeals into together flow in product-collecting bucket with water of condensation, after this, product is stayed in product-collecting bucket, and water of condensation enters in water of condensation temporary storage barrel from product-collecting bottom of the barrel by pipeline outflow;
Second step, after borneol camphor tree branches and leaves have distilled, has been taken out, and is discharged by the liquid in still pot, and in still pot, is reentered into new borneol camphor tree branches and leaves;
3rd step: the water of condensation that the first step water of condensation temporary storage barrel is collected is pumped into bottom still pot, then, the ball valve at the place that switches off the pump, refunds to water of condensation to prevent the water of condensation in still pot and stores temporarily in bucket; Then open the second steam control valve, the water of condensation entered in still pot is heated, distilled, originally the natural Broneolum Syntheticum dissolved and be suspended in water of condensation and borneol oil are distilled away, the natural Broneolum Syntheticum distilled out and borneol oil are with the borneol camphor tree branches and leaves layer of steam by new loading, and enter into condenser with the natural Broneolum Syntheticum that distills from the borneol camphor tree branches and leaves of new clothes and borneol oil with steam and carry out condensation, in product-collecting bucket, then reclaim the natural Broneolum Syntheticum again entered wherein and borneol oil.
4th step: the water of condensation in still pot through after a while (distillation time general control was at 20 to 30 minutes) distillation after, just can by dissolve and be suspended in water of condensation natural Broneolum Syntheticum distillation complete.And the steam that water of condensation produces in still-process in still pot also just in time completes the heating of new clothes borneol camphor tree branches and leaves and the process to excluding air in water distilling apparatus simultaneously, just directly enter into the process that new clothes borneol camphor tree branches and leaves are distilled.
5th step: after above-mentioned 4th step end of processing, open the wash water valve (being also liquid discharge pipe) bottom still pot, the water of condensation not containing natural Broneolum Syntheticum in still pot can be discharged, emptying containing after the water of condensation of natural Broneolum Syntheticum, does not close wash water valve.Then, slowly closing second steam control valve and open the first steam control valve, close the second steam control valve and open the first steam control valve and will carry out simultaneously, in the process of above-mentioned two valve conversions, keep the pressure in still pot substantially constant, prevent the steam in pot from spraying from its still pot water seal or the water in water seal is sucked in pot, after two valve conversions, steam is passed into the steam distributor in still pot by the first steam control valve, steam is evenly distributed in still pot by steam distributor, distills new clothes borneol camphor tree branches and leaves.
6th step: just other organism shovel on the natural Broneolum Syntheticum on condenser inner wall and its can be collected to product-collecting bucket every 4 to 8 pots, so far, the production of this batch terminates.The production of next batch from second step to the 6th EOS.Circulate successively.
Original water of condensation of draining as waste water is sent in still pot and is carried out distillation process by the present invention, reclaims natural Broneolum Syntheticum wherein, improves the recovery rate of natural Broneolum Syntheticum.
Native system adopts in Ji'an, Jiangxi company 2014 annual whole production cycle (on January 15,24 days to 2015 November in 2014) this extraction system and method to carry out the extraction work of natural Broneolum Syntheticum, the production data sufficient proof of the said firm ideal effect of the present invention.
Table 12014 annual borneol output statistics table (unit: ㎏)
Table 1 is 2014 annual borneol output statistics tables, can find out from upper table data: from water of condensation, reclaim the forward and backward equal pot borneol output of natural Broneolum Syntheticum obviously different.On large level ground, hill does not reclaim the natural Broneolum Syntheticum in water of condensation, equal pot borneol output is 1.456kg, the natural Broneolum Syntheticum in water of condensation has been reclaimed on the pheasant pool, Lao Wushan, Yi Jialing, my humble abode hill, equal pot borneol output is 1.754kg, after natural Broneolum Syntheticum in water of condensation reclaims, equal pot natural Broneolum Syntheticum output increased 20.47%.
Pass through native system, when existing equipment, production time, production cost are constant, a small amount of fund is spent to increase a set of condensate water recovery device, natural Broneolum Syntheticum in water of condensation and some other organism (such as borneol oil) are all reclaimed, do not produce any waste, thoroughly solve environmental issue again.Meanwhile, native system U-shaped pressure gauge for micropressure used replaces spring loaded tensimeter directly to measure pressure in still pot, thus the pressure that can control more directly perceived, more convenient, more accurately in still pot and steam flow.After adopting native system and method, all problems existed in existing system and method is fundamentally resolved, its investment is simultaneously little, has high repayment.The present invention, except for extracting except natural Broneolum Syntheticum and borneol oil from borneol camphor tree branches and leaves, can be used for all in principle and adopting steam distillation to extract in the production technology of product.
Meanwhile, native system and method do not need to transform existing cooling system again, do not need to carry out automatic improving to steam flow Controlling System and control method yet, have saved many improvement expenseses.
What embodiment of the present utility model was announced is preferred embodiment; but be not limited thereto; those of ordinary skill in the art; very easily according to above-described embodiment; understand spirit of the present utility model; and make different amplifications and change, but only otherwise depart from spirit of the present utility model, all in protection domain of the present utility model.
Claims (9)
1. one kind can be improved the natural Broneolum Syntheticum extraction system of recovery rate, it comprises in bottom it the still pot and the condenser that be communicated with corresponding to the vapour outlet of described still pot that are provided with steam distributor, and the steam inlet of the steam distributor in this still pot is communicated with by saturated vapor pipeline is corresponding with saturated vapor producer; It is characterized in that: it also comprises a water of condensation temporary storage barrel for being carried out reclaiming by the water of condensation after condenser condenses; Described water of condensation temporary storage barrel is also communicated with the inside of described still pot by water pump, to be delivered in still pot by the water of condensation collected in water of condensation temporary storage barrel by described water pump.
2. can improve the natural Broneolum Syntheticum extraction system of recovery rate as claimed in claim 1, it is characterized in that: also comprise the product-collecting bucket which is provided with bung, the outlet of described condenser and the inlet communication of this product-collecting bucket; One is also provided with for the water outlet by the water of condensation discharge in this product-collecting bucket at the middle part of described product-collecting bucket, and a vertically disposed pipeline is provided with in this product-collecting bucket, the upper end of this pipeline is communicated with described water outlet, at the bottom of the lower end of this pipeline is arranged at barrel; Be communicated with via a drainage element is corresponding with described water of condensation temporary storage barrel with the water outlet that described pipeline upper end is communicated with; Described drainage element is without blocking diversion trench; Describedly comprise without blocking diversion trench the lower U-lag main body and upper U-lag groove lid that its section all takes the shape of the letter U, described upper U-lag groove cover buckle in described lower U-lag main body, so that the passage formed between the two is formed condensation flow circulation passage.
3. can improve the natural Broneolum Syntheticum extraction system of recovery rate as claimed in claim 1, it is characterized in that: also offer water of condensation import in the bottom of described still pot; Described water of condensation temporary storage barrel is communicated with by water pump is corresponding with described water of condensation import.
4. can improve the natural Broneolum Syntheticum extraction system of recovery rate as claimed in claim 3, it is characterized in that: described saturated vapor pipeline is also corresponding with described water of condensation import to be communicated with, and pipeline between described saturated vapor pipeline and described water of condensation import is also provided with the second steam control valve.
5. can improve the natural Broneolum Syntheticum extraction system of recovery rate as claimed in claim 1, it is characterized in that: the saturated vapor pipeline that the steam distributor in described still pot is communicated with steam generating stove is also provided with the first steam control valve.
6. can improve the natural Broneolum Syntheticum extraction system of recovery rate as claimed in claim 5, it is characterized in that: on the saturated vapor pipeline of described first steam control valve admission end, also be provided with tensimeter.
7. can improve the natural Broneolum Syntheticum extraction system of recovery rate as claimed in claim 5, it is characterized in that: on the inwall of described still pot middle and lower part, also be provided with the first pressure tap, this first pressure tap is communicated with by the first pressure measurement control valve is corresponding with minute-pressure measuring cell; The saturated vapor pipeline of described first steam control valve steam output end offers the second pressure tap, and this second pressure tap is communicated with by the second pressure measurement control valve is also corresponding with described minute-pressure measuring cell.
8. can improve the natural Broneolum Syntheticum extraction system of recovery rate as claimed in claim 7, it is characterized in that: described minute-pressure measuring cell comprise in it fill liquid and the transparent tube arranged that takes the shape of the letter U, and by retaining plate fixing for described transparent tube; And also scale marks is provided with along in the vertical direction of described transparent tube on described retaining plate; One end of described transparent tube is communicated with described first pressure measurement control valve is corresponding with the second pressure measurement control valve by tee pipe fitting, its other end opening.
9. can improve the natural Broneolum Syntheticum extraction system of recovery rate as claimed in claim 3, it is characterized in that: the water of condensation ingress bottom described still pot is also provided with the liquid discharge pipe of being discharged by the liquid in this still pot, and is also provided with discharge opeing control valve on this liquid discharge pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520893292.6U CN205088156U (en) | 2015-11-11 | 2015-11-11 | Can improve natural borneol extraction system who receives yield |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520893292.6U CN205088156U (en) | 2015-11-11 | 2015-11-11 | Can improve natural borneol extraction system who receives yield |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205088156U true CN205088156U (en) | 2016-03-16 |
Family
ID=55478861
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520893292.6U Active CN205088156U (en) | 2015-11-11 | 2015-11-11 | Can improve natural borneol extraction system who receives yield |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205088156U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105237358A (en) * | 2015-11-11 | 2016-01-13 | 江西玉霞山农业开发有限公司 | Natural borneol extraction system and method capable of increasing yield |
| CN108484358A (en) * | 2018-04-27 | 2018-09-04 | 泉州市泉美生物科技有限公司 | A method of extracting natural d-borneol from camphor tree branches and leaves |
| CN113149815A (en) * | 2021-05-13 | 2021-07-23 | 安徽右旋龙脑生物科技有限公司 | Extraction system and extraction method of high-purity borneol |
-
2015
- 2015-11-11 CN CN201520893292.6U patent/CN205088156U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105237358A (en) * | 2015-11-11 | 2016-01-13 | 江西玉霞山农业开发有限公司 | Natural borneol extraction system and method capable of increasing yield |
| CN108484358A (en) * | 2018-04-27 | 2018-09-04 | 泉州市泉美生物科技有限公司 | A method of extracting natural d-borneol from camphor tree branches and leaves |
| CN113149815A (en) * | 2021-05-13 | 2021-07-23 | 安徽右旋龙脑生物科技有限公司 | Extraction system and extraction method of high-purity borneol |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205088156U (en) | Can improve natural borneol extraction system who receives yield | |
| CN104606909B (en) | One kind of plant Oleum sesami boiler | |
| CN101266102A (en) | Cane sugar factory waste water zero discharge process | |
| CN104848284A (en) | Steam condensation water heat recovery method and device | |
| CN102952629A (en) | Technological method for extracting natural cinnamon oil | |
| CN202061411U (en) | Backflow extraction concentration unit | |
| CN105237358A (en) | Natural borneol extraction system and method capable of increasing yield | |
| CN206089622U (en) | High accuracy flower bud of lily magnolia flower extraction of essential oil device | |
| CN205576059U (en) | Distilling and extracting device for plant essential oil | |
| CN212560169U (en) | Plant volatile oil extraction device | |
| CN102584524A (en) | Alcohol recovery tower | |
| CN103007572A (en) | Medicine extraction device and technique thereof | |
| CN201186168Y (en) | Multifunctional machine group for refluxing, extracting and concentrating | |
| CN205031921U (en) | Strip tower flash steam's heat energy and solvent recycling system | |
| CN209113847U (en) | A kind of Rosa Damascana extraction element facilitating collection | |
| CN201334471Y (en) | Blumea balsamifera powder extracting device | |
| CN202892957U (en) | Extraction and collection device | |
| CN203030013U (en) | Solvent recovery and water removal device for sucralose production | |
| KR101872491B1 (en) | Vacuum circulation type extraction equipment | |
| CN205449572U (en) | Asphalitine extraction device | |
| CN204854387U (en) | Condenser | |
| CN212581826U (en) | Pyrolysis gas segmentation processing system | |
| CN103706142B (en) | A kind of extraction collection device and application thereof | |
| CN106433984B (en) | A kind of equipment for extraction of essential oil | |
| CN216244213U (en) | Condensate water closed flash steam overflow-free recovery unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160608 Address after: West Industrial Park 331600 Ji'an city of Jiangxi province Jishui county two Ji Chang Lu Patentee after: Jiangxi Jinggang Natural Medicine Co., Ltd. Address before: 343000 Ji'an province Jiangxi City Qingyuan Road on the eastern side Everising spring No. 51 1-201 Patentee before: JIANGXI YUXIASHAN AGRICULTURE DEVELOPMENT CO., LTD. |