CN205461110U - Erythritol's continuous crystallization device - Google Patents
Erythritol's continuous crystallization device Download PDFInfo
- Publication number
- CN205461110U CN205461110U CN201620264027.6U CN201620264027U CN205461110U CN 205461110 U CN205461110 U CN 205461110U CN 201620264027 U CN201620264027 U CN 201620264027U CN 205461110 U CN205461110 U CN 205461110U
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- erythritol
- continuous
- outer tube
- nucleation system
- utility
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Abstract
The utility model particularly relates to an erythritol's continuous crystallization device specifically includes erythritol dissolving kettle (8), continuous nucleation system, mixes the suspension and mixes ejection of compact crystallizer (7), dissolves the pipe connection of analysing between agent reinforced cauldron (6) and the above -mentioned equipment. The utility model discloses the continuous nucleation system that erythritol's continuous crystallization device adopted is a two -layer same pipe spreader, analyses agent and erythritol's flash mixed through intraductal exsolution, but the intraductal outflow velocity ratio of accessible regulation and control is gone back to the stable crystal seed of production quality (crystal seed quantity and particle size distribution ) not only, produces anticipated quality and particle size distribution's crystal seed conveniently. Compare in traditional erythritol intermittent type crystallization equipment, the utility model discloses still have low, the advantages such as rate of equipment utilization is high, loading and unloading capacity is big, degree of automation height of running cost.
Description
Technical field
This utility model belongs to industrial crystallization technical field, is specifically related to the continuous crystallisation device of a kind of erythritol.
Background technology
Erythritol is a kind of novel polyalcohols Functional sweetening agents and natural saccharic, and the metabolic characteristics of its uniqueness makes it be known as " zero calorie ", and diabetics is suitable for.Erythritol also has without cariogenic tooth；High dosis tolerata, side effect is little, mouthfeel is good；It is difficult to cause gastrointestinal upset；Stable to heat and acid, routinely food processing do not have the advantage such as brown stain and decomposing phenomenon.Therefore, erythritol be widely used, the market demand big.
The production technology of erythritol mainly has chemical synthesis and fermentation method, is finally both needed to use Crystallization Separation technology, could obtain erythritol product.At present, the crystallization processes that erythritol produces is mainly periodic crystallisation operation, such as evaporative crystallization, crystallisation by cooling and dilution crystallization.Compared to batch crystallization process, continuous crystallisation is steady state operation, has that running cost is low, utilization rate of equipment and installations is high, production capacity is big, automaticity advantages of higher.And, state Behavior of Continuous Crystallization Processes constant product quality, the differences between batches phenomenon of batch crystallization process product quality can be prevented effectively from.Additionally, continuous crystallisation also has, procedure parameter is easy to control, be more easy to realize the advantages such as industry amplification.
Summary of the invention
This utility model is intended to overcome above-mentioned technological deficiency, it is provided that the continuous crystallisation device of a kind of erythritol.
For achieving the above object, the continuous crystallisation device of this utility model erythritol, specifically include erythritol dissolution kettle (8), continuous nucleation system, mix suspending mixing discharging crystallizer (7), dissolved agent coppers (6), between described erythritol dissolution kettle (8) and continuous nucleation system, between dissolved agent coppers (6) and continuous nucleation system, the pipeline being provided by pump (5) between dissolved agent coppers (6) with mix suspending mixing discharging crystallizer (7) respectively is connected, it is connected by pipeline between described continuous nucleation system with mix suspending mixing discharging crystallizer (7).
Described continuous nucleation system is a two-layer coaxial sleeve, including outer tube (1), inner tube (2), tubulose upper shield (3) and feed tube (4), inner tube (2) is through in outer tube (1), upper shield (3) one end is welded with outer tube (1), gap between sealed inner tube (2) and outer tube (1) after other end reducing, feed tube (4) described in inlet connection is set on upper shield (3) sidewall, the other end opening of sleeve pipe, and the difference of the length of outer tube (1) and inner tube (2) is 10～30 times of outer tube (1) diameter.
Described erythritol dissolution kettle (8) is the jacketed stirred tank of controllable temperature.
Described dissolved agent coppers (6) is the jacketed stirred tank of controllable temperature.
Owing to using technique scheme, this utility model compared with prior art has a following good effect:
(1) the continuous crystallisation device of the erythritol involved by this utility model, compared to traditional periodic crystallisation device, belongs to steady state operation, has that running cost is low, utilization rate of equipment and installations is high, production capacity is big, automaticity advantages of higher；The differences between batches phenomenon of batch crystallization process product quality can be prevented effectively from.
(2) the continuous crystallisation device of the erythritol involved by this utility model, have employed continuous nucleation system, the crystal seed that quality (crystal seed quantity and particle size distribution) is stable can be continuously produced in whole crystallization process, in addition, flow velocity by erythritol solution in regulation and control continuous nucleation system with dissolved agent, it is also possible to produce the crystal seed of prospective quality and particle size distribution easily.
Accompanying drawing explanation
Fig. 1 is this utility model schematic diagram.
Detailed description of the invention
The utility model is further explained below in conjunction with the accompanying drawings explanation, the not restriction to its protection domain.
As shown in Figure 1, the continuous crystallisation device of the erythritol involved by this utility model, specifically include erythritol dissolution kettle (8), continuous nucleation system, mix suspending mixing discharging crystallizer (7), dissolved agent coppers (6), between described erythritol dissolution kettle (8) and continuous nucleation system, between dissolved agent coppers (6) and continuous nucleation system, the pipeline being provided by pump (5) between dissolved agent coppers (6) with mix suspending mixing discharging crystallizer (7) respectively is connected, it is connected by pipeline between described continuous nucleation system with mix suspending mixing discharging crystallizer (7).
Described continuous nucleation system is a two-layer coaxial sleeve, including outer tube (1), inner tube (2), tubulose upper shield (3) and feed tube (4), inner tube (2) is through in outer tube (1), upper shield (3) one end is welded with outer tube (1), gap between sealed inner tube (2) and outer tube (1) after other end reducing, feed tube (4) described in inlet connection is set on upper shield (3) sidewall, the other end opening of sleeve pipe, and the difference of the length of outer tube (1) and inner tube (2) is 10～30 times of outer tube (1) diameter.
The continuous crystallisation device implementation process describing erythritol involved by this utility model in conjunction with concrete technology operating condition is as follows: 10～80 DEG C and 100～500r/min speed conditions under, erythritol and water are hybridly prepared into the erythritol solution that concentration is 50 ~ 80wt%；Erythritol solution is sent into the feed tube (4) of continuous nucleation system I again, and the dissolved agent of 10～80 DEG C is divided into two bursts of inner tubes (2) being respectively fed to continuous nucleation system I closing side and continuous crystallizing system II simultaneously, maintain the constant liquid level in crystallizer, discharge continuously magma to carry out filtering, wash, be dried, prepare erythritol crystal product.
In described continuous nucleation system I inner tube (2), dissolved agent flow velocity is outer tube (1) mesoerythrit solution flow rate (0.01 ~ 0.05) times.
Described dissolved agent is ethanol.
Total stream rate of acceleration of described dissolved agent is continuous nucleation system I outer tube (1) mesoerythrit solution flow rate (1.0 ~ 1.2) times.
In described crystallizer, the mean residence time of erythritol is 1 ~ 5 hour.
Claims (4)
1. the continuous crystallisation device of an erythritol, it is characterized in that, specifically include erythritol dissolution kettle (8), continuous nucleation system, mix suspending mixing discharging crystallizer (7), dissolved agent coppers (6), between described erythritol dissolution kettle (8) and continuous nucleation system, between dissolved agent coppers (6) and continuous nucleation system, the pipeline being provided by pump (5) between dissolved agent coppers (6) with mix suspending mixing discharging crystallizer (7) respectively is connected, it is connected by pipeline between described continuous nucleation system with mix suspending mixing discharging crystallizer (7).
The continuous crystallisation device of erythritol the most according to claim 1, it is characterized in that, described continuous nucleation system is a two-layer coaxial sleeve, including outer tube (1), inner tube (2), tubulose upper shield (3) and feed tube (4), inner tube (2) is through in outer tube (1), upper shield (3) one end is welded with outer tube (1), gap between sealed inner tube (2) and outer tube (1) after other end reducing, feed tube (4) described in inlet connection is set on upper shield (3) sidewall, the other end opening of sleeve pipe, and the difference of the length of outer tube (1) and inner tube (2) is 10～30 times of outer tube (1) diameter.
The continuous crystallisation device of erythritol the most according to claim 1, it is characterised in that described erythritol dissolution kettle (8) is the jacketed stirred tank of controllable temperature.
The continuous crystallisation device of erythritol the most according to claim 1, it is characterised in that described dissolved agent coppers (6) is the jacketed stirred tank of controllable temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620264027.6U CN205461110U (en) | 2016-04-01 | 2016-04-01 | Erythritol's continuous crystallization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620264027.6U CN205461110U (en) | 2016-04-01 | 2016-04-01 | Erythritol's continuous crystallization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205461110U true CN205461110U (en) | 2016-08-17 |
Family
ID=56646222
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620264027.6U Expired - Fee Related CN205461110U (en) | 2016-04-01 | 2016-04-01 | Erythritol's continuous crystallization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205461110U (en) |
-
2016
- 2016-04-01 CN CN201620264027.6U patent/CN205461110U/en not_active Expired - Fee Related
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160817 Termination date: 20170401 |