CN103537104A - Fructose-glucose syrup evaporating system - Google Patents
Fructose-glucose syrup evaporating system Download PDFInfo
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- CN103537104A CN103537104A CN201310512366.2A CN201310512366A CN103537104A CN 103537104 A CN103537104 A CN 103537104A CN 201310512366 A CN201310512366 A CN 201310512366A CN 103537104 A CN103537104 A CN 103537104A
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- surge tank
- tank body
- evaporator
- hfcs
- tank
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Abstract
The invention discloses a fructose-glucose syrup evaporating system relating to the field of food additive manufacture and being designed for solving the problems that the traditional fructose-glucose syrup production process is not easy to control and the like. The fructose-glucose syrup evaporating system comprises a controller and an evaporating tank, wherein the evaporating tank comprises an evaporating tank body; the top of the evaporating tank body is provided with an evaporating tank material inlet, and the bottom of the evaporating tank body is provided with an evaporating tank material outlet; the front end of the evaporating tank is also provided with a feeding buffer tank comprising a buffer tank body; the buffer tank body is provided with a buffer tank material inlet and a buffer tank material outlet; the buffer tank material outlet is connected with the evaporating tank material inlet through a flow regulating valve; the controller is connected with the flow regulating valve. The fructose-glucose syrup evaporating system can be used for ensuring the stability of the production process of fructose-glucose syrup.
Description
Technical field
The present invention relates to food additives and manufacture field, relate in particular to a kind of HFCS vapo(u)rization system.
Background technology
HFCS is a kind of product that can substitute sucrose completely, and be widely used in food and beverage industry, particularly application in beverage industry the same as sucrose, and its local flavor and mouthfeel are better than sucrose.The rise of Price of Sugar, makes the application of HFCS in the industry such as food, beverage show advantage fully.Produce HFCS and be not subject to area and season limit, comparison in equipment is simple, and investment cost is lower.
The production technology of HFCS comprises liquefaction, saccharification, isomerization and concentrated, in concentration technology, finally needs refining liquid glucose to be concentrated into required concentration through evaporator, thereby obtains HFCS finished product.Because the volume of evaporator is limited, the speed of each production process before evaporation technology is mated with the evaporation rate of evaporator is bad, and production process is not easy control, affects production efficiency.
Summary of the invention
An object of the present invention is to propose a kind of HFCS vapo(u)rization system that can guarantee HFCS stable production process.
A further object of the present invention is the HFCS vapo(u)rization system that proposes a kind of effective raising HFCS concentration precision.
For reaching this object, the present invention by the following technical solutions:
A kind of HFCS vapo(u)rization system, comprise controller and evaporator, described evaporator comprises evaporator tank body, evaporator tank body top is provided with evaporator material inlet, evaporator tank base is provided with evaporator material outlet, the front end of described evaporator is also provided with charging surge tank, and described charging surge tank comprises surge tank tank body, is provided with surge tank material inlet and surge tank material outlet on surge tank tank body;
Described surge tank material outlet is connected with described evaporator material inlet by flow control valve, and described controller connects described flow control valve.
Preferably, on described surge tank tank body, be also provided with feed back mouth, described evaporator material outlet connects described feed back mouth by feed back pipeline;
On described feed back pipeline, be provided with reversal valve, the input of described reversal valve connects described evaporator material outlet, and two outputs of described reversal valve connect respectively material refluxing opening and material output pipe;
Near described evaporator material outlet, be also provided with the concentration tester for detection of evaporator material outlet place HFCS concentration;
Described controller connects described reversal valve and described concentration tester.
Preferably, described concentration tester is arranged on described evaporator tank body;
Or described concentration tester is arranged on described feed back pipeline and between described reversal valve and described evaporator material outlet.
Preferably, described surge tank material inlet and described feed back mouth are arranged at the top of described surge tank tank body, and described surge tank material outlet is arranged at the bottom of described surge tank tank body.
Preferably, the top of described surge tank tank body is also provided with soft water import, and described soft water import is connected with soft water supply device.
Preferably, on described charging surge tank, be provided with liquid level gauge, the sidepiece of described surge tank tank body has liquid level gauge mouth, and described liquid level gauge is penetrated in described surge tank tank body by described liquid level gauge mouth.
Preferably, on described charging surge tank, be provided with fluid level transmitter, the sidepiece of described surge tank tank body has fluid level transmitter mouth, and described fluid level transmitter is penetrated in described surge tank tank body by described fluid level transmitter mouth.
Preferably, the bottom of described surge tank tank body is tapered.
Preferably, the top of described surge tank tank body and sidepiece are for removably connecting, and the top of described surge tank tank body is provided with handle.
Preferably, the top of described surge tank tank body is connected with the sidepiece of described surge tank tank body by hinges.
Beneficial effect of the present invention is:
(1) HFCS vapo(u)rization system of the present invention was provided with charging surge tank before surge tank, first HFCS to be evaporated after process premenstruum (premenstrua) enters charging surge tank, by charging surge tank, entering evaporator again evaporates, therefore, each production process of HFCS before evaporation technology is not subject to the impact of evaporator evaporation rate, and by the charging rate of Flow-rate adjustment valve regulation evaporator, make the production process of HFCS more stable by controller.
(2) be also provided with feed back pipeline, when the HFCS concentration in evaporator exit does not reach requirement, HFCS flows back to charging surge tank through feed back pipeline, proceeds evaporation process, has guaranteed the precision of HFCS concentration.
(3) bottom of surge tank tank body is tapered, is convenient to the outflow of HFCS to be evaporated.
Accompanying drawing explanation
Fig. 1 is the structural representation of the HFCS vapo(u)rization system that provides of the embodiment of the present invention one;
Fig. 2 is the top view of the charging surge tank that provides of the embodiment of the present invention one;
Fig. 3 is the structural representation of the HFCS vapo(u)rization system that provides of the embodiment of the present invention two.
In figure, 1, evaporator; 11, evaporator tank body; 12, evaporator material inlet; 13, evaporator material outlet; 2, charging surge tank; 21, surge tank tank body; 22, handle; 23, surge tank material inlet; 24, feed back mouth; 25, soft water import; 26, liquid level gauge mouth; 27, fluid level transmitter mouth; 28, surge tank material outlet; 3, controller; 4, soft water supply device; 5, liquid level gauge; 6, fluid level transmitter; 7, flow control valve; 8, feed back pipeline; 9, reversal valve; 10, material output pipe; 14, concentration tester.
The specific embodiment
Below in conjunction with accompanying drawing and by the specific embodiment, further illustrate technical scheme of the present invention.
Embodiment mono-:
Fig. 1 is the structural representation of the HFCS vapo(u)rization system that provides of the present embodiment.As shown in the figure, this HFCS vapo(u)rization system comprises evaporator 1, charging surge tank 2 and controller 3.
On charging surge tank 2, be provided with liquid level gauge 5, the sidepiece of surge tank tank body 21 has liquid level gauge mouth 26, and liquid level gauge 5 is penetrated in surge tank tank body 21 by liquid level gauge mouth 26.On charging surge tank 2, be provided with fluid level transmitter 6, the sidepiece of surge tank tank body 21 has fluid level transmitter mouth 27, and fluid level transmitter 6 is penetrated in surge tank tank body 21 by fluid level transmitter mouth 27.For convenience of the outflow of HFCS to be evaporated, the bottom of surge tank tank body 21 is tapered.
When HFCS vapo(u)rization system is worked, HFCS to be evaporated is flowed in charging surge tank 2 and is carried out buffer storage by surge tank material inlet 23, controller 3 is controlled HFCS to be evaporated by flow control valve 7 and through surge tank material outlet 28 and evaporator material inlet 12, is flowed into the inflow velocity of evaporator 1, HFCS after evaporation process is flowed out by evaporator material outlet 13, when through concentration tester 14, concentration tester 14 transfers to controller 3 by the concentration value of the HFCS detecting, controller 3 judges whether to meet or exceed required HFCS concentration, if, the output of reversal valve 9 is changed to material output pipe 10, otherwise the output of reversal valve 9 is changed to feed back mouth 24, proceed evaporation process, effectively guaranteed the precision of end product HFCS concentration.
HFCS vapo(u)rization system of the present invention was provided with charging surge tank before surge tank, first HFCS to be evaporated after process premenstruum (premenstrua) enters charging surge tank, by charging surge tank, entering evaporator again evaporates, therefore, each production process of HFCS before evaporation technology is not subject to the impact of evaporator evaporation rate, and by the charging rate of Flow-rate adjustment valve regulation evaporator, make the production process of HFCS more stable by controller.
Wherein, the top of surge tank tank body is not limited to by hinges and is connected with the sidepiece of surge tank tank body, can realize other syndetons for convenience detach and all can.
Embodiment bis-:
Fig. 3 is the structural representation of the present embodiment HFCS vapo(u)rization system.As shown in the figure, the basic structure of the present embodiment HFCS vapo(u)rization system is identical with embodiment mono-, comprises controller 3, charging surge tank 2 and evaporator 1.Difference is, the reversal valve 9 of the present embodiment directly connects evaporator material outlet 13, and concentration tester 14 is arranged on evaporator tank body 11 bottoms near the position of evaporator material outlet 13.
The course of work of the present embodiment HFCS vapo(u)rization system is identical with embodiment mono-.
Know-why of the present invention has below been described in conjunction with specific embodiments.These are described is in order to explain principle of the present invention, and can not be interpreted as by any way limiting the scope of the invention.Explanation based on herein, those skilled in the art does not need to pay performing creative labour can associate other specific embodiment of the present invention, within these modes all will fall into protection scope of the present invention.
Claims (10)
1. a HFCS vapo(u)rization system, comprise controller (3) and evaporator (1), described evaporator (1) comprises evaporator tank body (11), evaporator tank body (11) top is provided with evaporator material inlet (12), evaporator tank body (11) bottom is provided with evaporator material outlet (13), it is characterized in that: the front end of described evaporator (1) is also provided with charging surge tank (2), described charging surge tank (2) comprises surge tank tank body (21), on surge tank tank body (21), be provided with surge tank material inlet (23) and surge tank material outlet (28),
Described surge tank material outlet (28) is connected with described evaporator material inlet (12) by flow control valve (7), and described controller (3) connects described flow control valve (7).
2. a kind of HFCS vapo(u)rization system according to claim 1, it is characterized in that: on described surge tank tank body (21), be also provided with feed back mouth (24), described evaporator material outlet (13) connects described feed back mouth (24) by feed back pipeline (8);
On described feed back pipeline (8), be provided with reversal valve (9), the input of described reversal valve (9) connects described evaporator material outlet (13), and two outputs of described reversal valve (9) connect respectively material refluxing opening (24) and material output pipe (10);
Near described evaporator material outlet (13), be also provided with the concentration tester (14) of locating HFCS concentration for detection of evaporator material outlet (13);
Described controller (3) connects described reversal valve (9) and described concentration tester (14).
3. a kind of HFCS vapo(u)rization system according to claim 2, is characterized in that: described concentration tester (14) is arranged on described evaporator tank body (11);
Or described concentration tester (14) is arranged on described feed back pipeline (8) above and is positioned between described reversal valve (9) and described evaporator material outlet (13).
4. according to a kind of HFCS vapo(u)rization system described in claims 1 to 3 any one, it is characterized in that: described surge tank material inlet (23) and described feed back mouth (24) are arranged at the top of described surge tank tank body (21), and described surge tank material outlet (28) is arranged at the bottom of described surge tank tank body (21).
5. a kind of HFCS vapo(u)rization system according to claim 4, is characterized in that: the top of described surge tank tank body (21) is also provided with soft water import (25), and described soft water import (25) is connected with soft water supply device (4).
6. according to a kind of HFCS vapo(u)rization system described in claims 1 to 3 any one, it is characterized in that: on described charging surge tank (2), be provided with liquid level gauge (5), the sidepiece of described surge tank tank body (21) has liquid level gauge mouth (26), and described liquid level gauge (5) is penetrated in described surge tank tank body (21) by described liquid level gauge mouth (26).
7. according to a kind of HFCS vapo(u)rization system described in claims 1 to 3 any one, it is characterized in that: on described charging surge tank (2), be provided with fluid level transmitter (6), the sidepiece of described surge tank tank body (21) has fluid level transmitter mouth (27), and described fluid level transmitter (6) is penetrated in described surge tank tank body (21) by described fluid level transmitter mouth (27).
8. a kind of HFCS vapo(u)rization system according to claim 1, is characterized in that: the bottom of described surge tank tank body (21) is tapered.
9. a kind of HFCS vapo(u)rization system according to claim 1, is characterized in that: the top of described surge tank tank body (21) and sidepiece are for removably connecting, and the top of described surge tank tank body (21) is provided with handle (22).
10. a kind of HFCS vapo(u)rization system according to claim 9, is characterized in that: the top of described surge tank tank body (21) is connected with the sidepiece of described surge tank tank body (21) by hinges.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310512366.2A CN103537104A (en) | 2013-10-25 | 2013-10-25 | Fructose-glucose syrup evaporating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310512366.2A CN103537104A (en) | 2013-10-25 | 2013-10-25 | Fructose-glucose syrup evaporating system |
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| CN103537104A true CN103537104A (en) | 2014-01-29 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201310512366.2A Pending CN103537104A (en) | 2013-10-25 | 2013-10-25 | Fructose-glucose syrup evaporating system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105002308A (en) * | 2015-07-29 | 2015-10-28 | 广西农垦糖业集团防城精制糖有限公司 | Method for preventing syrup from being overrich or being scorched |
| CN107879362A (en) * | 2016-09-29 | 2018-04-06 | 内蒙古乌海化工有限公司 | A kind of induction system for evaporation of chlorine-alkali |
Citations (10)
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| SU1227236A1 (en) * | 1984-03-27 | 1986-04-30 | Stavash Aleksandr K | Method of concentrating viscous liquids |
| JPH01262800A (en) * | 1988-04-11 | 1989-10-19 | Taisei Sangyo Kk | Method and apparatus for concentrating sugar syrup |
| CN201492953U (en) * | 2008-08-05 | 2010-06-02 | 贵阳铝镁设计研究院 | Plate-type evaporating tank |
| CN201519474U (en) * | 2009-09-25 | 2010-07-07 | 上海瑞派机械有限公司 | External circulating evaporator |
| CN101966396A (en) * | 2010-09-21 | 2011-02-09 | 广州市心德实业有限公司 | Evaporation device |
| CN201942687U (en) * | 2011-01-11 | 2011-08-24 | 安徽友勇生物科技有限公司 | System for automatically controlling discharge concentration of evaporation section of syrup |
| CA2770478A1 (en) * | 2011-03-11 | 2012-09-11 | Tole Inox Inc. | Method and system for controlling liquid levels |
| CN102698445A (en) * | 2012-06-04 | 2012-10-03 | 浙江温兄机械阀业有限公司 | Automatic control water bath evaporation unit |
| CN103007561A (en) * | 2012-12-17 | 2013-04-03 | 西王药业有限公司 | Concentration production technology for glucose liquid |
| CN203577338U (en) * | 2013-10-25 | 2014-05-07 | 昆山市盛兴设备安装有限公司 | High fructose corn syrup evaporation system |
-
2013
- 2013-10-25 CN CN201310512366.2A patent/CN103537104A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1227236A1 (en) * | 1984-03-27 | 1986-04-30 | Stavash Aleksandr K | Method of concentrating viscous liquids |
| JPH01262800A (en) * | 1988-04-11 | 1989-10-19 | Taisei Sangyo Kk | Method and apparatus for concentrating sugar syrup |
| CN201492953U (en) * | 2008-08-05 | 2010-06-02 | 贵阳铝镁设计研究院 | Plate-type evaporating tank |
| CN201519474U (en) * | 2009-09-25 | 2010-07-07 | 上海瑞派机械有限公司 | External circulating evaporator |
| CN101966396A (en) * | 2010-09-21 | 2011-02-09 | 广州市心德实业有限公司 | Evaporation device |
| CN201942687U (en) * | 2011-01-11 | 2011-08-24 | 安徽友勇生物科技有限公司 | System for automatically controlling discharge concentration of evaporation section of syrup |
| CA2770478A1 (en) * | 2011-03-11 | 2012-09-11 | Tole Inox Inc. | Method and system for controlling liquid levels |
| CN102698445A (en) * | 2012-06-04 | 2012-10-03 | 浙江温兄机械阀业有限公司 | Automatic control water bath evaporation unit |
| CN103007561A (en) * | 2012-12-17 | 2013-04-03 | 西王药业有限公司 | Concentration production technology for glucose liquid |
| CN203577338U (en) * | 2013-10-25 | 2014-05-07 | 昆山市盛兴设备安装有限公司 | High fructose corn syrup evaporation system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105002308A (en) * | 2015-07-29 | 2015-10-28 | 广西农垦糖业集团防城精制糖有限公司 | Method for preventing syrup from being overrich or being scorched |
| CN107879362A (en) * | 2016-09-29 | 2018-04-06 | 内蒙古乌海化工有限公司 | A kind of induction system for evaporation of chlorine-alkali |
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Application publication date: 20140129 |