CN204767461U - Quick enrichment facility of suspension - Google Patents
Quick enrichment facility of suspension Download PDFInfo
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- CN204767461U CN204767461U CN201520381386.5U CN201520381386U CN204767461U CN 204767461 U CN204767461 U CN 204767461U CN 201520381386 U CN201520381386 U CN 201520381386U CN 204767461 U CN204767461 U CN 204767461U
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- concentration
- suspension
- concentrated
- heater
- high pressure
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Abstract
The utility model relates to a quick enrichment facility of suspension, the device includes the concentration jar, and concentration jar outside is equipped with the high pressure pre -heater of suspension, is equipped with the coil pipe in the high pressure pre -heater, and the one end and the liquid outlet of treating concentrated suspension storage tank of coil pipe are connected, and the other end and the setting of coil pipe are connected at the atomizer of concentrated tank deck portion, and the top of concentration jar still is equipped with the gas vent, and the gas vent passes through the blast pipe to be connected with vapour and liquid separator, and the bottom of concentrated jar is equipped with the concentrate calandria, and the concentrate calandria is connected with concentrate recovery jar, the atomizer of concentrated tank deck portion is provided with a plurality ofly, and at the top of equipartition concentrated jar still be equipped with pressure regulator at concentrated jar top, be equipped with the foam shielding plate at pressure regulator's lower extreme the upper portion of high pressure pre -heater is equipped with steam heating section or electrical heating section. Quick enrichment facility of suspension has concentrated fastly, and concentration effect is good, energy -conservation, the characteristics such as operation of being convenient for.
Description
Technical field
The utility model relates to liquid concentrator technical field, is specifically related to a kind of suspension rapid concentration device.
Background technology
The concentrated dilute aqueous solution (suspension) generally referred to containing a certain amount of solute, insoluble suspendible solid (particulate), loses the process that a part of aqueous solvent obtains denseer solution (suspension).In fact concentration process can be that the part that certain energy (heat) input makes aqueous solvent evaporate is separated, to improve the process of solute, suspended matter relative amount in residue concentrate.The concentrated part in fact also comprising solvent solute in non-aqueous solution (suspension) of broad sense is separated.
Concentration operation is widely used in chemical industry, food, beverage, medicine and other fields, and existing method has different classification according to different sorting techniques, as: can be divided into according to operating pressure that normal pressure is concentrated, reduced pressure concentration; According to the motion mode of weak solution (suspension), be divided into tribe Cimicifugeae, falling film concentration; According to the feature of liquid evaporating surface, be divided into surface to concentrate, seething with excitement concentrates etc.
Concentration process is actually the part evaporation of aqueous solvent, and the water evaporation properties at different conditions of utilization is carried out.Conventional principle has: reduce pressure (reduced pressure concentration), reduces boiling point, improves evaporation efficiency; Reduce the concentration of concentration process evaporated vapor, improve vapour concentration difference (draining steam, steam in time), improve evaporation rate; Increase disengagement area (film concentrates), improve disengagement area.
Common concentrator has: uncovered concentration pan, single-action multiple-effect vacuum concentration tank, thin film concentrator, tubular type Centrifugal concentrators etc., the Rotary Evaporators that laboratory is conventional in addition.
In above-mentioned concentration process, the behavior of the solution (suspension) of per unit volume has two kinds of motion modes: one is that the liquid of all units accepts energy (heat) input in the lump, all unit liquid almost evaporate simultaneously, terminate until concentrated; Two is that a concentrated unit volume solution carries out, and namely certain volume liquid depart from concentration process after completing and concentrating, and next part liquid continues concentrated, departs from ... until all volume of liquid complete concentration process.The former can be called hot concentration process altogether; After then can be called non-co-thermal process.
Heat is one of chemical change major contributory factor, and therefore, concentration process is more short better with heated time, avoids composition wherein that undesirable chemical change occurs, and is conducive to reducing energy resource consumption simultaneously.Therefore, the hot concentration process of above-mentioned non-co-is a kind of mode that hot concentration process is good comparatively altogether.Therefore, to concentrate quality good for the concentrated more general single-effect vacuum concentration tank of the film of tubular type.
In addition, in order to improve the utilization ratio of the energy, the concentrated steam (indirect steam) produced can recycle, for heating other a part of liquid.
Therefore, improve the eliminating speed that concentrated speed critical is to reduce evaporation boiling point, improve evaporating surface, improve steam (gas), and the utilization of indirect steam.
Utility model content
The purpose of this utility model is to overcome defect of the prior art, designs a kind of suspension rapid concentration device heating liquid to be concentrated at concentration tank outward in advance.
For achieving the above object, the technical scheme that the utility model adopts is:
A kind of suspension rapid concentration device, it is characterized in that, described device comprises concentration tank, concentration tank outside is provided with the high pressure pre-heater of suspension, coil pipe is provided with in high pressure pre-heater, one end of coil pipe is connected with the liquid outlet of suspension storage tank to be concentrated, the other end of coil pipe is connected with the atomizer being arranged on concentration tank top, the top of concentration tank is also provided with exhaust outlet, exhaust outlet is connected with gas-liquid separator by blast pipe, the bottom of concentration tank is provided with concentrate comb, and concentrate comb is connected with concentrate recycling can.
In order to increase the surface area of large concentrated liquid, preferred technical scheme is, the atomizer at described concentration tank top is provided with multiple, and at the top being distributed on concentration tank.
In order to avoid foam and foreign material enter gas-liquid separator, preferred technical scheme also has, and is also provided with pressure regulator, is provided with foam shutter in the lower end of pressure regulator at the described top at concentration tank.
Be fully utilized to make heat energy, preferred technical scheme also has further, the exhaust outlet of described gas-liquid separator is connected to the bottom of high pressure pre-heater by pipeline, and forms the second coil pipe in its underpart, and the other end of the second coil pipe is connected to the outside of high pressure pre-heater.
In order to simplify the structure of heater, improve the efficiency of heating surface, preferred technical scheme also has further, is provided with steam heating segment or electric heater section on the top of described high pressure pre-heater.
Concentrate the concentration levels of rear liquid for the ease of observing and controlling, preferred technical scheme also has further, is also provided with sample tap in the bottom of described concentration tank.
Advantage of the present utility model and beneficial effect are: it is fast that described suspension rapid concentration device has concentrated speed, and concentrated effect is good, energy-conservation, the features such as convenient operation.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model suspension rapid concentration device.
In figure: 1, concentration tank; 2, high pressure pre-heater; 3, coil pipe; 4, suspension storage tank to be concentrated; 5, liquid outlet; 6, atomizer; 7, blast pipe; 8, gas-liquid separator; 9, concentrate comb; 10, concentrate recycling can; 11, pressure regulator; 12, foam shutter; 13, sample tap.
Detailed description of the invention
Below in conjunction with drawings and Examples, detailed description of the invention of the present utility model is further described.Following examples only for clearly the technical solution of the utility model being described, and can not limit protection domain of the present utility model with this.
As shown in Figure 1: a kind of suspension rapid concentration device, described device comprises concentration tank 1, the outside of concentration tank 1 is provided with the high pressure pre-heater 2 of suspension, coil pipe 3 is provided with in high pressure pre-heater 2, one end of coil pipe 3 is connected with the liquid outlet 5 of suspension storage tank 4 to be concentrated, the other end of coil pipe 3 is connected with the atomizer 6 being arranged on concentration tank 1 top, the top of concentration tank 1 is also provided with exhaust outlet, exhaust outlet is connected with gas-liquid separator 8 by blast pipe 7, the bottom of concentration tank 1 is provided with concentrate comb 9, and concentrate comb 9 is connected with concentrate recycling can 10.
The utility model is in order to increase the surface area of large concentrated liquid, and preferred embodiment is, the atomizer 6 at described concentration tank 1 top is provided with multiple, and is being distributed on the top of concentration tank 1.
The utility model enters gas-liquid separator 8 in order to avoid foam and foreign material, and preferred embodiment also has, and is also provided with pressure regulator 11, is provided with foam shutter 12 in the lower end of pressure regulator at the described top at concentration tank 1.
The utility model is fully utilized to make heat energy, further preferred embodiment also has, the exhaust outlet of described gas-liquid separator 8 is connected to the bottom of high pressure pre-heater 2 by pipeline, and the second coil pipe (not shown) is formed in its underpart, the other end of the second coil pipe is connected to the outside of high pressure pre-heater 2.
The utility model, in order to simplify the structure of heater, improves the efficiency of heating surface, and further preferred embodiment also has, and is provided with steam heating segment or electric heater section on the top of described high pressure pre-heater 2.
The utility model concentrates the concentration levels of rear liquid for the ease of observing and controlling, and further preferred embodiment also has, and is also provided with sample tap 13 in the bottom of described concentration tank 1.
The above is only preferred embodiment of the present utility model; should be understood that; for those skilled in the art; under the prerequisite not departing from the utility model know-why; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (6)
1. a suspension rapid concentration device, it is characterized in that, described device comprises concentration tank, concentration tank outside is provided with the high pressure pre-heater of suspension, coil pipe is provided with in high pressure pre-heater, one end of coil pipe is connected with the liquid outlet of suspension storage tank to be concentrated, the other end of coil pipe is connected with the atomizer being arranged on concentration tank top, the top of concentration tank is also provided with exhaust outlet, exhaust outlet is connected with gas-liquid separator by blast pipe, the bottom of concentration tank is provided with concentrate comb, and concentrate comb is connected with concentrate recycling can.
2. suspension rapid concentration device as claimed in claim 1, it is characterized in that, the atomizer at described concentration tank top is provided with multiple, and at the top being distributed on concentration tank.
3. suspension rapid concentration device as claimed in claim 2, is characterized in that, be also provided with pressure regulator, be provided with foam shutter in the lower end of pressure regulator at the described top at concentration tank.
4. suspension rapid concentration device as claimed in claim 3, it is characterized in that, the exhaust outlet of described gas-liquid separator is connected to the bottom of high pressure pre-heater by pipeline, and forms the second coil pipe in its underpart, and the other end of the second coil pipe is connected to the outside of high pressure pre-heater.
5. suspension rapid concentration device as claimed in claim 4, is characterized in that, be provided with steam heating segment or electric heater section on the top of described high pressure pre-heater.
6. suspension rapid concentration device as claimed in claim 5, is characterized in that, be also provided with sample tap in the bottom of described concentration tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520381386.5U CN204767461U (en) | 2015-06-04 | 2015-06-04 | Quick enrichment facility of suspension |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520381386.5U CN204767461U (en) | 2015-06-04 | 2015-06-04 | Quick enrichment facility of suspension |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204767461U true CN204767461U (en) | 2015-11-18 |
Family
ID=54507593
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520381386.5U Expired - Fee Related CN204767461U (en) | 2015-06-04 | 2015-06-04 | Quick enrichment facility of suspension |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204767461U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109499078A (en) * | 2019-01-17 | 2019-03-22 | 柳三春 | It can accelerate the solution method of evaporating of evaporation rate |
-
2015
- 2015-06-04 CN CN201520381386.5U patent/CN204767461U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109499078A (en) * | 2019-01-17 | 2019-03-22 | 柳三春 | It can accelerate the solution method of evaporating of evaporation rate |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151118 Termination date: 20160604 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |