CN208857301U - A kind of seaweed sugar production system - Google Patents
A kind of seaweed sugar production system Download PDFInfo
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- CN208857301U CN208857301U CN201820952153.XU CN201820952153U CN208857301U CN 208857301 U CN208857301 U CN 208857301U CN 201820952153 U CN201820952153 U CN 201820952153U CN 208857301 U CN208857301 U CN 208857301U
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Abstract
The application discloses a kind of seaweed sugar production system, comprising: catalytic unit；The import department being set on catalytic unit and outlet portion；The enzyme preparation feedway being connected to import department；The pure water being connected to import department weighs and Dropping feeder；The decoloration device being connected to outlet portion；The ion-exchange system being connect with decoloration device；The concentration systems being connect with ion-exchange system；The crystallization apparatus being connect with concentration systems；The crystallization discharging portion for exporting trehalose is provided on crystallization apparatus.A kind of seaweed sugar production system provided by the present application, compared with prior art, automated production ability with higher, while labor intensity is greatly reduced, production efficiency also greatly improves compared with prior art.
Description
Technical field
This application involves trehalose production technical fields, more specifically more particularly to a kind of seaweed sugar production system.
Background technique
Trehalose is a kind of safe and reliable natural carbohydrate, is to be made of two glucose molecules with 1,1- glycosidic bond
Nonreducing sugar.There are 3 kinds of isomers i.e. trehalose (α, α), isotrehalose (β, β) and neotrehalose (α, β).It is living to a variety of biologies
Property substance there is non-specific protective effect.A large amount of research with practice have shown that, trehalose can be effectively protected epidermal cell film
Structure, activating cell improve skin, enable skin health natural, flexible.Epidermal cell is in high temperature, high and cold, dry, strong ultraviolet
It under the environment such as beta radiation, easily dries out and makes skin damage, trehalose can be formed in this case in cell surface
One layer of special protective film keeps the original nutrition of skin and moisture, avoids skin sunburn and melanin deposition, be effective against skin
Aging phenomenon；The mucus being precipitated from film can mild moisturizing, make bright skin jade-like stone, gloss, tender.
Currently, since trehalose discovery is not also for a long time that production technology is also immature, in the prior art, the life of trehalose
The deficiencies of production process has the degree of automation low, and production efficiency is low place, the safety of production system are to be improved.
Therefore it provides a kind of seaweed sugar production system, high degree of automation, high production efficiency, security of system is strong,
Become those skilled in the art's technical problem urgently to be resolved.
Utility model content
In order to solve the above technical problems, the application provides a kind of seaweed sugar production system, high degree of automation, production effect
Rate is high, and security of system is strong.
Technical solution provided by the present application is as follows:
A kind of seaweed sugar production system, comprising: catalytic unit；The import department being set on catalytic unit and outlet portion；With
The enzyme preparation feedway of import department's connection；The pure water being connected to import department weighs and Dropping feeder；It is connected to outlet portion
Decoloration device；The ion-exchange system being connect with decoloration device；The concentration systems being connect with ion-exchange system；The knot being connect with concentration systems
Brilliant device；The crystallization discharging portion for exporting trehalose is provided on crystallization apparatus.
Further, in a kind of preferred mode of the utility model, decoloration device connect tool with outlet portion, ion-exchange system
Body are as follows: decoloration sheet frame in decoloration device is connect by the pump that decolourizes with outlet portion, the filter press discharge port in decoloration device and from
Friendship system is connected.
Further, in a kind of preferred mode of the utility model, concentration systems include: by ion-exchange pump and ion-exchange system
Tank before the concentration of system connection；By concentration feed pump and preceding tank connected inspissator is concentrated；After the concentration being connect with crystallization apparatus
Tank, tank is connect with inspissator discharge port after concentration.
Further, in a kind of preferred mode of the utility model, tank is connect with ion-exchange system before being concentrated specifically: from
With tank before ion-exchange and ion-exchange column in friendship system；Ion-exchange column includes positive post and negative column；The outlet of tank is connected with before the ion-exchange
Two heat exchangers, second heat exchanger are connected with the positive post, and the outlet of positive post is connected with negative column import, and the outlet of negative column passes through
Ion-exchange pump is connected with preceding tank is concentrated.
Further, in a kind of preferred mode of the utility model, tank is connect with crystallization apparatus after concentration specifically: dense
The discharge port of tank is connected with crystallization feed pump after contracting, and crystallization feed pump is connected with First Heat Exchanger, and First Heat Exchanger and crystallization fill
The feed inlet set is connected.
Further, it in a kind of preferred mode of the utility model, is equipped on tank after tank, concentration before being concentrated: manhole；
For being closed the manhole cover of manhole；Be installed on manhole cover close to switch.
Further, in a kind of preferred mode of the utility model, speed reducer rabbling mechanism is equipped in catalytic unit；It urges
Makeup sets steam pipe coil in setting；Steam in catalytic unit, which enters, is equipped with pressure gauge on pipe；Catalytic unit is equipped with plug-in type
Temperature measuring mechanism；The shut-off valve for adjusting air inflow is additionally provided in catalytic unit.
Further, in a kind of preferred mode of the utility model, seaweed sugar production system further include: for being filled to catalysis
Set the active carbon addition mechanism of interior addition active carbon；Starch sugar for adding from crystal starch sugar to catalytic unit adds machine
Structure.
Further, there is water pot, sour tank, alkali tank in a kind of preferred mode of the utility model, in ion-exchange system；Water
Tank, sour tank, alkali tank are made of polythene material.
A kind of seaweed sugar production system provided by the utility model, compared with prior art, comprising: catalytic unit, catalysis
Device is equipped with import department and outlet portion, and import department weighs with enzyme preparation feedway and pure water and is connected to Dropping feeder,
Outlet portion is connected to decoloration device, and decoloration device is connected with ion-exchange system, and ion-exchange system is connected with concentration systems, and concentration systems connect
It is connected to crystallization apparatus, the crystallization discharging portion for exporting trehalose is provided on crystallization apparatus.Trehalose provided by the present application is raw
Production system, compared to existing technologies, the degree of automation is significantly improved with production efficiency, and security of system significantly increases.
Detailed description of the invention
In order to illustrate the technical solutions in the embodiments of the present application or in the prior art more clearly, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
Some embodiments of application for those of ordinary skill in the art without creative efforts, can be with
It obtains other drawings based on these drawings.
Fig. 1 is the schematic diagram of seaweed sugar production system provided by the embodiment of the utility model；
Fig. 2 is the schematic diagram of ion-exchange system provided by the embodiment of the utility model.
Specific embodiment
In order to make those skilled in the art more fully understand the technical solution in the application, the application will be implemented below
Technical solution in example is clearly and completely described, it is clear that described embodiment is only that a part of the application is implemented
Example, instead of all the embodiments.Based on the embodiment in the application, those of ordinary skill in the art are not making creativeness
Every other embodiment obtained, shall fall in the protection scope of this application under the premise of labour.
Please be as shown in Figure 1 to Figure 2, seaweed sugar production system includes: catalytic unit 4；The import being set on catalytic unit 4
Portion and outlet portion；The enzyme preparation feedway being connected to import department；The pure water being connected to import department weighs and Dropping feeder 1；
The decoloration device being connected to outlet portion；The ion-exchange system 10 being connect with decoloration device；The concentration systems being connect with ion-exchange system 10；
The crystallization apparatus 18 being connect with concentration systems；The crystallization discharging portion for exporting trehalose is provided on crystallization apparatus 18.
Seaweed sugar production system provided by the embodiment of the utility model, compared with prior art, catalytic unit 4, catalysis dress
It sets 4 and is equipped with import department and outlet portion, import department weighs with enzyme preparation feedway and pure water and is connected to Dropping feeder 1,
Outlet portion is connected to decoloration device, and decoloration device is connected with ion-exchange system 10, and ion-exchange system 10 is connected with concentration systems, concentration system
System is connected with crystallization apparatus 18, and the crystallization discharging portion for exporting trehalose is provided on crystallization apparatus 18.It is provided by the present application
Seaweed sugar production system, compared to existing technologies, the degree of automation is significantly improved with production efficiency, and security of system is aobvious
Write enhancing.
Specifically, in the utility model embodiment, decoloration device is connect with outlet portion, ion-exchange system 10 specifically: de-
Decoloration sheet frame in color device is connect by decoloration pump 7 with outlet portion, 8 discharge port of filter press in decoloration device and ion-exchange system
10 are connected.
Specifically, in the utility model embodiment, concentration systems include: to be connect by ion-exchange pump 20 with ion-exchange system 10
Concentration before tank 12；The inspissator 14 being connect by concentration feed pump 13 with tank 12 before concentration；It is connect with crystallization apparatus 18 dense
Tank 15 after contracting, tank 15 is connect with 14 discharge port of inspissator after concentration.
Specifically, in the utility model embodiment, tank 12 is connect with ion-exchange system 10 before being concentrated specifically: ion-exchange system
With tank 19 before ion-exchange and ion-exchange column 23 in 10；Ion-exchange column 23 includes positive post and negative column；Being connected with for tank 19 second is changed before ion-exchange
Hot device 21, the second heat exchanger 21 are connected with positive post, and the outlet of positive post is connected with negative column import, and the outlet of negative column passes through ion-exchange pump 20
It is connected with preceding tank 12 is concentrated.
Specifically, in the utility model embodiment, tank 15 is connect with crystallization apparatus 18 after concentration specifically: tank after concentration
15 discharge port is connected with crystallization feed pump 16, and crystallization feed pump 16 is connected with First Heat Exchanger 17, First Heat Exchanger 17 and knot
The feed inlet of brilliant device 18 is connected.Specifically, First Heat Exchanger 17 and the second heat exchanger 21 are plate heat exchanger.
Specifically, it in the utility model embodiment, is equipped on tank 15 after tank 12, concentration before being concentrated: manhole；For closing
Close the manhole cover 2 of manhole；Be installed on manhole cover 2 close to switch 3.
Specifically, in the utility model embodiment, speed reducer rabbling mechanism is equipped in catalytic unit 4；In catalytic unit 4
If steam pipe coil 5；Steam in catalytic unit 4, which enters, is equipped with pressure gauge on pipe；Catalytic unit 4 is equipped with plug-in type temperature measuring machine
Structure；The shut-off valve for adjusting air inflow is additionally provided in catalytic unit 4.
In the present embodiment, 4 kinds of catalytic unit of catalyzing tank is stirred using motor reducer, and motor uses electrodeless frequency conversion tune
Speed, built-in coil pipe lead to steam, fill pressure gauge, shut-off valve on steam inlet tube, control air inflow, catalyzing tank by adjustable cut-off valve
On be associated with plug-in type temperature measuring point, by adjustable cut-off valve control air inflow, adjust catalyzing tank inside temperature.
Specifically, in the utility model embodiment, Automatic stop switch is installed, Automatic stop switch is for incuding on filter press 8
Feed pressure controls 8 operation suspension of filter press when reaching setting value.In the present embodiment, the charging of the filter press 8 of decoloration device
Pressure realizes that filter press is specially plate type pressure filter in the present embodiment using the motor by frequency control feed pump, this
Outer this system is additionally provided with decoloration plate type pressure filter travel control device 9.
Specifically, in the utility model embodiment, seaweed sugar production system further include: for adding into catalytic unit 4
The active carbon of active carbon is added to add mechanism；Starch sugar for adding from crystal starch sugar to catalytic unit 4 adds mechanism；It can also
Using manually to the manhole of catalyzing tank addition active carbon and crystal starch sugar.
Specifically, there is water pot 26, sour tank 25, alkali tank 27 in the utility model embodiment, in ion-exchange system 10；Water pot
26, sour tank 25, alkali tank 27 are made of polythene material.Flowmeter 24 is connected between ion-exchange tank and ion-exchange column 23, using frequency conversion
Self priming pump 28 is controlled, the flow for flowing to PE material ion-exchange column 23 is accurately controlled.
It further include PLC control device 11 in seaweed sugar production system, for controlling seaweed in the utility model embodiment
The operation conditions of each device in sugar production system, in addition, further including operating platform 6, enzyme preparation supply in seaweed sugar production system
Device, pure water weighing may be provided at Dropping feeder 1, decoloration device, ion-exchange system 10, concentration systems, crystallization apparatus 18
On operating platform 6；Seaweed sugar production system further includes waste liquid transfer device, and waste liquid transfer device includes more PE material storage tanks,
PE material storage tank is connect with device by hose with waste liquid, and valve is equipped at connector；The present embodiment is in ion-exchange system
The injury of equipment and personnel is avoided using Frequency Converter Control using highly basic and strong acid self priming pump 28 in 10.
The seaweed sugar production system that the utility model embodiment is related to is because will use strong bronsted lowry acids and bases bronsted lowry, ion-exchange system 10 in production
In water pot 26, alkali tank 27 and sour tank 25 and other function type tank body all use the PE material of acid and alkali-resistance, involved in system
Feed pipe on be mounted on electrical ball valve 22, highly basic and strong acid self priming pump 28 are used in ion-exchange system 10, using frequency converter control
System can avoid the injury of equipment and personnel as far as possible, reduce the accident frequency rate in production, sea provided in this embodiment
Algae sugar production system automated production ability with higher, while labor intensity is greatly reduced, production efficiency and existing skill
Art is compared and is also greatly improved.
The foregoing description of the disclosed embodiments can be realized professional and technical personnel in the field or using originally practical new
Type.Various modifications to these embodiments will be readily apparent to those skilled in the art, and determine herein
The General Principle of justice can be realized in other embodiments without departing from the spirit or scope of the present utility model.Cause
This, the present invention will not be limited to the embodiments shown herein, and is to fit to and principles disclosed herein
The widest scope consistent with features of novelty.
Claims (9)
1. a kind of seaweed sugar production system characterized by comprising catalytic unit；The import being set on the catalytic unit
Portion and outlet portion；The enzyme preparation feedway being connected to the import department；The pure water being connected to the import department weighs and drop
Feeder apparatus；The decoloration device being connected to the outlet portion；The ion-exchange system being connect with the decoloration device；With the ion-exchange system
The concentration systems of connection；The crystallization apparatus being connect with the concentration systems；It is provided on the crystallization apparatus for exporting seaweed
The crystallization discharging portion of sugar.
2. seaweed sugar production system according to claim 1, which is characterized in that the decoloration device and the outlet portion,
The ion-exchange system connection specifically: the decoloration sheet frame in the decoloration device is connect by the pump that decolourizes with the outlet portion, institute
The filter press discharge port stated in decoloration device is connected with the ion-exchange system.
3. seaweed sugar production system according to claim 1, which is characterized in that the concentration systems include: to pass through ion-exchange
Tank before the concentration that pump is connect with the ion-exchange system；Pass through tank connected inspissator before concentration feed pump and the concentration；With institute
State crystallization apparatus connection concentration after tank, tank is connect with the inspissator discharge port after the concentration.
4. seaweed sugar production system according to claim 3, which is characterized in that tank and the ion-exchange system before the concentration
Connection specifically: there is tank and ion-exchange column before ion-exchange in ion-exchange system；The ion-exchange column includes positive post and negative column；Before the ion-exchange
The outlet of tank is connected with the second heat exchanger, and second heat exchanger is connected with the positive post, the outlet of the positive post and the yin
Column import is connected, and the outlet of the yin column is pumped by the ion-exchange to be connected with tank before the concentration.
5. seaweed sugar production system according to claim 4, which is characterized in that tank and the crystallization apparatus after the concentration
Connection specifically: the discharge port of tank is connected with crystallization feed pump after the concentration, and the crystallization feed pump is connected with the first heat exchange
Device, the First Heat Exchanger are connected with the feed inlet of the crystallization apparatus.
6. seaweed sugar production system according to claim 5, which is characterized in that tank after tank, the concentration before the concentration
On be equipped with: manhole；For being closed the manhole cover of the manhole；Be installed on the manhole cover close to switch.
7. seaweed sugar production system according to claim 6, which is characterized in that stirred in the catalytic unit equipped with speed reducer
Mix mechanism；Steam pipe coil is set in the catalytic unit；Steam in the catalytic unit, which enters, is equipped with pressure gauge on pipe；It is described
Catalytic unit is equipped with plug-in type temperature measuring mechanism；The shut-off valve for adjusting air inflow is additionally provided in the catalytic unit.
8. according to claim 1 to seaweed sugar production system described in 7 any one, which is characterized in that the trehalose production
System further include: the active carbon for adding active carbon into the catalytic unit adds mechanism；For to the catalytic unit
The starch sugar of interior addition crystal starch sugar adds mechanism.
9. according to claim 1 to seaweed sugar production system described in 7 any one, which is characterized in that in the ion-exchange system
With water pot, sour tank, alkali tank；The water pot, the sour tank, the alkali tank are made of polythene material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820952153.XU CN208857301U (en) | 2018-06-20 | 2018-06-20 | A kind of seaweed sugar production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820952153.XU CN208857301U (en) | 2018-06-20 | 2018-06-20 | A kind of seaweed sugar production system |
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| CN208857301U true CN208857301U (en) | 2019-05-14 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201820952153.XU Active CN208857301U (en) | 2018-06-20 | 2018-06-20 | A kind of seaweed sugar production system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110698572A (en) * | 2019-10-25 | 2020-01-17 | 福建天源兴达生物科技有限公司 | Running water type agar production line |
-
2018
- 2018-06-20 CN CN201820952153.XU patent/CN208857301U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110698572A (en) * | 2019-10-25 | 2020-01-17 | 福建天源兴达生物科技有限公司 | Running water type agar production line |
| CN110698572B (en) * | 2019-10-25 | 2021-11-02 | 福建天源兴达生物科技有限公司 | Running water type agar production line |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220707 Address after: 421800 Building 1, Dongjiang Industrial Park, baiyangdu Neighborhood Committee Economic Development Zone, sanjai street, Leiyang City, Hengyang City, Hunan Province Patentee after: Hunan Jindai Technology Development Co.,Ltd. Address before: 421800 Building 1, Dongjiang Industrial Park, Leiyang Economic Development Zone, Hengyang City, Hunan Province Patentee before: HUNAN HUISHENG BIOTECHNOLOGY Co.,Ltd. |
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| TR01 | Transfer of patent right |