CN109865304A - The extraction process and extraction element of more substances in a kind of solution - Google Patents
The extraction process and extraction element of more substances in a kind of solution Download PDFInfo
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- CN109865304A CN109865304A CN201711323945.7A CN201711323945A CN109865304A CN 109865304 A CN109865304 A CN 109865304A CN 201711323945 A CN201711323945 A CN 201711323945A CN 109865304 A CN109865304 A CN 109865304A
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Abstract
The present invention relates to the extraction processes and extraction element of material in a kind of solution.Specific extraction step is that raw material flows through booster pump pressurization by storage tank and enters gasifying pot, and is atomized by atomizer；Gasifying pot outer layer is heating layer, controls to adjust valve towards control system control hot water and controls hot water flow, and control heating layer reaches 30~100 DEG C, is heated, is kept the temperature to internal gasifying pot；The raw material of atomization speeds up to realize vaporization to the substance of extraction, enters condenser by top steam guiding tube, be condensed out finished product and store because the latent heat of vaporization of different material is different；It is not easy the water vaporized simultaneously and falls into tank bottom through gravity, carries out subsequent processing after importing exhausted bath box.
Description
Technical field:
The present invention relates to the extraction processes and extraction element of material in a kind of solution.
Background technique:
Existing more material mixing solution usually utilize different material boiling point different, are extracted in a manner of distillation, this
Mode is all by the way of completely heated up, and energy consumption is big, and can not operate continuously.
Summary of the invention:
The present invention is exactly in view of the above-mentioned problems, providing the extraction process and extraction element of more substances in a kind of solution.
To achieve the goals above, the present invention adopts the following technical scheme that, specific extraction step is,
1, raw material flows through booster pump pressurization into gasifying pot by storage tank, and is atomized by atomizer；
2, gasifying pot outer layer is heating layer, controls to adjust valve towards control system control hot water and controls to hot water flow
System, control heating layer reach 30~100 DEG C, are heated, kept the temperature to internal gasifying pot；
3, the raw material being atomized speeds up to realize vaporization to the substance of extraction, by top because of the latent heat of vaporization difference of different material
Steam guiding tube enters condenser, is condensed out finished product and stores；It is not easy the water vaporized simultaneously and falls into tank bottom through gravity, after importing exhausted bath box
Carry out subsequent processing.
Extraction element includes storage tank, feed line, gasifying pot, hot water water inlet pipe, hot water outlet pipe, hot water control tune
Valve, atomizer, exhausted bath box, gas-guide tube, condenser, cooling water water inlet pipe, cooling water outlet pipe, cooling water control is saved to adjust
Valve, finished product delivery pipe, finished product storage tank and control system, storage tank are connected by feed line with the bottom of gasifying pot,
The exit of feed line is arranged in atomizer, and the bottom of gasifying pot also passes through sewer pipe and is connected with exhausted bath box；Vaporization
Be coated with heating layer on the outer wall of tank, be flowing hot water in heating layer, hot water water inlet pipe, hot water outlet pipe respectively with heating layer
It is connected；The top of gasifying pot is connected by steam guiding tube with the top of condenser, and the lower part of condenser passes through finished product delivery pipe
It is connected with finished product storage tank, it is the cold water of flowing in cooling layer that the interior pars intramuralis of condenser, which is cooling layer, cooling water water inlet pipe,
Cooling water outlet pipe wind is not connected with cooling layer；
Hot water controls to adjust valve, cooling water control regulating valve is connected to hot water water inlet pipe, on cooling water water inlet pipe, control
System processed controls to adjust valve with hot water respectively, the triggering end of cooling water control regulating valve is electrical connected, and realizes to control hot water and adjust
Save the control of valve, cooling water control regulating valve.
Be respectively connected with temperature sensor on heating layer outside gasifying pot, on condenser, control system respectively with two temperature
The triggering end of degree sensor is electrical connected, and realizes the control to temperature sensor.
It further include the booster pump on feed line, the triggering end of control system and booster pump is electrical connected, and realizes to increasing
The control of press pump.
The lower part of condenser is also communicated with exhaust impurity-discharging pipe.
Beneficial effects of the present invention:
1, the present invention accelerates convection current using heating air, and the substance evaporation for accelerating evaporation latent heat value low, and the latent heat of vaporization
High water reduces evaporation, realizes the extraction to predetermined substance, avoids the energy wasted by distilled water.
2, the present invention realizes that process continuous production, extraction efficiency are high in controlled range.
3, the present invention avoids raw caused by manual operation because of the vapo(u)rizing temperature of the specified extraction of substance of control system intelligent control
Production accident.
Detailed description of the invention:
Fig. 1 is the structural diagram of the present invention.
In Fig. 1,1 is storage tank, and 2 be booster pump, and 3 control to adjust valve for hot water, and 4 be atomizer, and 5 be heating layer, and 6 are
Exhausted bath box, 7 be control system, and 8 be finished product storage tank, and 9 be gasifying pot, and 10 be gas-guide tube, and 11 be temperature sensor, and 12 be condensation
Device, 13 be cooling water control regulating valve, and 14 be hot water water inlet pipe, and 15 be hot water outlet pipe, and 16 be cooling water outlet pipe, 17 at
Product delivery pipe, 18 be cooling water water inlet pipe.
Specific embodiment:
As shown in Figure 1, extraction step is that raw material flows through booster pump pressurization by storage tank and enters gasifying pot, and is sprayed by atomization
Mouth is atomized；Gasifying pot outer layer is heating layer, controls to adjust valve towards control system control hot water and controls to hot water flow
System, control heating layer reach 100 DEG C, are heated, kept the temperature to internal gasifying pot；The raw material of atomization is latent because of the vaporization of different material
It is hot different, vaporization is speeded up to realize to the substance of extraction, condenser is entered by top steam guiding tube, finished product is condensed out and stores；Simultaneously
It is not easy the water vaporized and falls into tank bottom through gravity, carry out subsequent processing after importing exhausted bath box.
Extraction element includes storage tank, feed line, gasifying pot, hot water water inlet pipe, hot water outlet pipe, hot water control tune
Valve, atomizer, exhausted bath box, gas-guide tube, condenser, cooling water water inlet pipe, cooling water outlet pipe, cooling water control is saved to adjust
Valve, finished product delivery pipe, finished product storage tank and control system, storage tank are connected by feed line with the bottom of gasifying pot,
The exit of feed line is arranged in atomizer, and the bottom of gasifying pot also passes through sewer pipe and is connected with exhausted bath box；Vaporization
Be coated with heating layer on the outer wall of tank, be flowing hot water in heating layer, hot water water inlet pipe, hot water outlet pipe respectively with heating layer
It is connected；The top of gasifying pot is connected by steam guiding tube with the top of condenser, and the lower part of condenser passes through finished product delivery pipe
It is connected with finished product storage tank, it is the cold water of flowing in cooling layer that the interior pars intramuralis of condenser, which is cooling layer, cooling water water inlet pipe,
Cooling water outlet pipe wind is not connected with cooling layer；
Hot water controls to adjust valve, cooling water control regulating valve is connected to hot water water inlet pipe, on cooling water water inlet pipe, control
System processed controls to adjust valve with hot water respectively, the triggering end of cooling water control regulating valve is electrical connected, and realizes to control hot water and adjust
Save the control of valve, cooling water control regulating valve.
Be respectively connected with temperature sensor on heating layer outside gasifying pot, on condenser, control system respectively with two temperature
The triggering end of degree sensor is electrical connected, and realizes the control to temperature sensor.
It further include the booster pump on feed line, the triggering end of control system and booster pump is electrical connected, and realizes to increasing
The control of press pump.
The lower part of condenser is also communicated with exhaust impurity-discharging pipe.
Claims (5)
1. the extraction process of more substances in a kind of solution, which is characterized in that specific extraction step is,
(1) raw material flows through booster pump pressurization into gasifying pot by storage tank, and is atomized by atomizer；
(2) gasifying pot outer layer is heating layer, controls to adjust valve towards control system control hot water and controls hot water flow, controls
Heating layer processed reaches 30~100 DEG C, is heated, is kept the temperature to internal gasifying pot；
(3) raw material being atomized speeds up to realize vaporization to the substance of extraction, by upper guide vapour because of the latent heat of vaporization difference of different material
Pipe enters condenser, is condensed out finished product and stores；It is not easy the water vaporized simultaneously and falls into tank bottom through gravity, is carried out after importing exhausted bath box
Subsequent processing.
2. the extraction element of more substances in a kind of solution described in claim 1, which is characterized in that defeated including storage tank, raw material
Pipe, gasifying pot, hot water water inlet pipe, hot water outlet pipe, hot water is sent to control to adjust valve, atomizer, exhausted bath box, gas-guide tube, condensation
Device, cooling water water inlet pipe, cooling water outlet pipe, cooling water control regulating valve, finished product delivery pipe, finished product storage tank and control system
System, storage tank are connected by feed line with the bottom of gasifying pot, and the exit of feed line is arranged in atomizer,
The bottom of gasifying pot also passes through sewer pipe and is connected with exhausted bath box；It is coated with heating layer on the outer wall of gasifying pot, is in heating layer
Flowing hot water, hot water water inlet pipe, hot water outlet pipe are connected with heating layer respectively；The top of gasifying pot by steam guiding tube with it is cold
The top of condenser is connected, and the lower part of condenser is connected by finished product delivery pipe with finished product storage tank, the interior pars intramuralis of condenser
For cooling layer, the interior cold water for flowing of cooling layer, cooling water water inlet pipe, cooling water outlet pipe wind are not connected with cooling layer.
3. the extraction element of more substances in solution according to claim 2, which is characterized in that hot water controls to adjust valve, cold
But water management regulating valve is connected to hot water water inlet pipe, on cooling water water inlet pipe, and control system is controlled to adjust with hot water respectively
Valve, cooling water control regulating valve triggering end be electrical connected, realize to hot water control to adjust valve, cooling water control regulating valve control
System.
4. the extraction element of more substances in solution according to claim 2, which is characterized in that the heating layer outside gasifying pot
It is respectively connected with temperature sensor on upper, condenser, triggering end of the control system respectively with two temperature sensors is electrical connected, real
Now to the control of temperature sensor.
5. the extraction element of more substances in solution according to claim 2, which is characterized in that further include on feed line
Booster pump, the triggering end of control system and booster pump is electrical connected, and realizes the control to booster pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711323945.7A CN109865304A (en) | 2017-12-01 | 2017-12-01 | The extraction process and extraction element of more substances in a kind of solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711323945.7A CN109865304A (en) | 2017-12-01 | 2017-12-01 | The extraction process and extraction element of more substances in a kind of solution |
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| CN109865304A true CN109865304A (en) | 2019-06-11 |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1118995A (en) * | 1993-03-06 | 1996-03-20 | 汉克尔股份两合公司 | Improved distillative separation process by steaming for mixtures of multiple substances |
| CN1994506A (en) * | 2006-01-06 | 2007-07-11 | 赖志勤 | Spray evaporation device/system |
| CN102120092A (en) * | 2010-12-17 | 2011-07-13 | 成都华融化工有限公司 | Spraying type solution evaporation and concentration method |
| CN104922929A (en) * | 2015-06-15 | 2015-09-23 | 湖北民族学院 | Natural medicine ultrasound continues extracting and concentrating device |
| CN105920861A (en) * | 2016-06-08 | 2016-09-07 | 燕山大学 | Spray distillation device |
| CN205627121U (en) * | 2016-05-24 | 2016-10-12 | 福建紫杉园生物有限公司 | Eluate enrichment facility of taxol is drawed to chinese yew |
| CN206447867U (en) * | 2017-01-23 | 2017-08-29 | 田高 | A kind of white wine intelligently distills impurities removal cooler |
-
2017
- 2017-12-01 CN CN201711323945.7A patent/CN109865304A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1118995A (en) * | 1993-03-06 | 1996-03-20 | 汉克尔股份两合公司 | Improved distillative separation process by steaming for mixtures of multiple substances |
| CN1994506A (en) * | 2006-01-06 | 2007-07-11 | 赖志勤 | Spray evaporation device/system |
| CN102120092A (en) * | 2010-12-17 | 2011-07-13 | 成都华融化工有限公司 | Spraying type solution evaporation and concentration method |
| CN104922929A (en) * | 2015-06-15 | 2015-09-23 | 湖北民族学院 | Natural medicine ultrasound continues extracting and concentrating device |
| CN205627121U (en) * | 2016-05-24 | 2016-10-12 | 福建紫杉园生物有限公司 | Eluate enrichment facility of taxol is drawed to chinese yew |
| CN105920861A (en) * | 2016-06-08 | 2016-09-07 | 燕山大学 | Spray distillation device |
| CN206447867U (en) * | 2017-01-23 | 2017-08-29 | 田高 | A kind of white wine intelligently distills impurities removal cooler |
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Application publication date: 20190611 |