CN203598508U - High fructose syrup triple-effect concentration evaporator - Google Patents
High fructose syrup triple-effect concentration evaporator Download PDFInfo
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- CN203598508U CN203598508U CN201320750501.2U CN201320750501U CN203598508U CN 203598508 U CN203598508 U CN 203598508U CN 201320750501 U CN201320750501 U CN 201320750501U CN 203598508 U CN203598508 U CN 203598508U
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- reboiler
- pump
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Abstract
The utility model discloses a high fructose syrup triple-effect evaporator which comprises a first evaporator, a second evaporator, a third evaporator, a material tank, an air pump, a cooling water tower, a vacuum pump and a finished product tank, wherein each evaporator comprises a reboiler and an evaporation chamber; the lower part of the reboiler is connected with the evaporation chamber; the bottom of the second reboiler is connected with the bottom of a second evaporation chamber and then led to a fourth material pump; and an outlet of the fourth material pump is led to the finished product tank. The high fructose syrup triple-effect evaporator disclosed by the utility model overcomes the shortcomings of low discharge efficiency and long discharge time of the existing single-effect evaporator, realizes continuous automatic operation and the best utilization of steam energy, has high production efficiency and is energy-saving and environment-friendly.
Description
Technical field
The utility model relates to by a technique in rice production HFCS, and more particularly it is a kind of HFCS Three-effect concentration evaporator.
Background technology
In the process with rice production HFCS, after Mashing process, the concentration of HFCS is all lower, only has 30% left and right, at present, in the time of the HFCS solution of production high concentration, normally the HFCS solution materials of low concentration is concentrated.The concentration technology of existing HFCS generally adopts single effect evaporator, and its vaporization chamber utilizes circulating pump to carry out forced circulation with the chamber of boiling again.The efficiency of the discharging of this technique is low, needs just can obtain for 45 minutes the HFCS of high concentration.
Summary of the invention
The purpose of this utility model is the deficiency existing in order to solve above-mentioned background technology, proposes a kind of HFCS Three-effect concentration evaporator.Its production efficiency is high, energy-conserving and environment-protective.
For achieving the above object, the designed HFCS triple effect evaporator of the utility model, it comprises the first evaporimeter, the second evaporimeter, the 3rd evaporimeter, material pot, cooling tower, vavuum pump, air pump, finished pot;
Described each evaporimeter includes a reboiler and a vaporization chamber, and the bottom of described reboiler is connected with described vaporization chamber;
The import of described air pump is connected with steam inlet tube, outlet is connected with the first reboiler, the overhead vapor outlet of the first vaporization chamber is connected with the second reboiler, the overhead vapor outlet of the second vaporization chamber is connected with the 3rd reboiler, the overhead vapor outlet of the 3rd vaporization chamber is connected with cooling tower, and the another side of cooling tower is connected with vavuum pump;
The import of described material pot is connected with material inlet pipe, outlet is connected with the first product pump, described the first material delivery side of pump is connected with the top of the 3rd reboiler, the bottom of the 3rd reboiler is connected to the second product pump with the bottom of the 3rd vaporization chamber, described the second material delivery side of pump is connected with the top of the first reboiler, the bottom of described the first reboiler is connected to 3 material pump with the bottom of the first vaporization chamber, described 3 material delivery side of pump is connected with the top of the second reboiler, the bottom of the second reboiler is connected to 4 materials pump with the bottom of the second vaporization chamber, described 4 materials delivery side of pump leads to finished pot.
The utility model has the advantage of:
1, after concentrated in the 3rd evaporimeter, HFCS flows into the first evaporimeter by product pump and concentrates, enters successively the second evaporimeter and concentrates purification, can obtain required finished product, sends into finished pot, has realized continuous automatic operation, and operating efficiency is high.
2, the concentrated heating vaporization of the first vaporization chamber produces steam and enters the second reboiler as its thermal source, and the concentrated heating vaporization of the second vaporization chamber produces steam and enters the 3rd reboiler as its thermal source, has realized the optimum utilization of steam energy, very energy-conserving and environment-protective.
Accompanying drawing explanation
Fig. 1 is HFCS Three-effect concentration evaporator structural representation.
In figure: material pot 1, the first product pump 2a, the second product pump 2b, 3 material pump 2c, 4 materials pump 2d, the first evaporimeter 3, the first reboiler 3a, the first vaporization chamber 3b, the second evaporimeter 4, the second reboiler 4a, the second vaporization chamber 4b, the 3rd evaporimeter 5, the 3rd reboiler 5a, the 3rd vaporization chamber 5b, air pump 6, cooling tower 7, vavuum pump 8, finished pot 9.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail:
Embodiment: HFCS triple effect evaporator as shown in the figure, is characterized in that it comprises three identical evaporimeters 3, material pot 1, air pump 6, cooling tower 7, vavuum pump 8, finished pot, 9;
Described each evaporimeter includes a reboiler and a vaporization chamber, and the bottom of described reboiler is connected with described vaporization chamber;
The import of described air pump 9 is connected with steam inlet tube, outlet is connected with the first evaporimeter reboiler 3a, the overhead vapor outlet of the first vaporization chamber 3b is connected with the second reboiler 4a, the overhead vapor outlet of the second vaporization chamber 4b is connected with the 3rd reboiler 5a, the overhead vapor outlet of the 3rd vaporization chamber 5b is connected with cooling tower 7, and the another side of cooling tower is connected with vavuum pump 8;
The import of described material pot 1 is connected with material inlet pipe, outlet is connected with the first product pump 2a, the outlet of described the first product pump 2a is connected with the top of the 3rd reboiler 5a, the bottom of the 3rd reboiler 5a is connected with the bottom of the 3rd vaporization chamber 5b to the second product pump 2b, the outlet of described the second product pump 2b is connected with the top of the first reboiler 3a, the bottom of described the first reboiler 3a is connected to 3 material pump (2c) with the bottom of the first vaporization chamber 3b, the outlet of described 3 material pump 2c is connected with the top of the second reboiler 4a, the bottom of the second reboiler 4a is connected to 4 materials pump 2d with the bottom of the second vaporization chamber 4b, finished pot 9 is led in the outlet of described 4 materials pump 2d.
The course of work of the present utility model is as follows: material enters material pot 1 by material inlet pipe, open thing the first product pump 2a by 30% HFCS solution suction the 3rd reboiler 5a of the concentration in material pot 1, at this by the Steam Heating from the second vaporization chamber 4b, HFCS Natural Circulation after heating enters the 3rd vaporization chamber 5b and carries out evaporation and concentration, water in HFCS is vaporized at the 3rd vaporization chamber 5b, water vapour is taken away and is entered cooling tower 7 by vavuum pump 8, discharges as condensed water, HFCS after the 3rd evaporimeter 5 is concentrated leads to the second product pump 2b by the 3rd reboiler 5a bottom and the 3rd vaporization chamber 5b bottom, by second product pump 2b suction the first reboiler 3a, at this by the Steam Heating from air pump 6, HFCS Natural Circulation after heating enters the first vaporization chamber 3b and carries out evaporation and concentration, in HFCS, the water of a part is vaporized at an effect vaporization chamber 3b, this vaporization chamber steam enters the second reboiler 4a as its thermal source, through the 3rd evaporimeter 6, HFCS after the first evaporimeter 3 is concentrated passes through 3 material pump 2c suction the second reboiler 4a by the first reboiler 3a bottom and vaporization chamber 3b bottom, at this by the Steam Heating from the first vaporization chamber 3b, HFCS Natural Circulation after heating enters the second vaporization chamber 4b and carries out evaporation and concentration, in HFCS, the water of a part is vaporized in the second vaporization chamber 4b, steam in this vaporization chamber enters the 3rd reboiler 5a as its thermal source, through the 3rd evaporimeter 6, the first evaporimeter 3, HFCS after the second evaporimeter 4 is concentrated, after whole three evaporimeters are concentrated, obtaining concentration is that 75% HFCS (mass percent concentration) enters finished pot 9, complete production.
The utility model utilizes the product pump between each single-effect evaporator, has realized the optimum utilization of steam energy, has realized continuous automatic operation.After concentrated in the 3rd evaporimeter, HFCS flows into the first evaporimeter by product pump and concentrates, enters successively the second evaporimeter and concentrates purification, can obtain required finished product, sends into finished pot, and operating efficiency is high; The concentrated heating vaporization of the first vaporization chamber produces steam and enters the second reboiler as its thermal source, and the concentrated heating vaporization of the second vaporization chamber produces steam and enters the 3rd reboiler as its thermal source, has realized the optimum utilization of steam energy, energy-conserving and environment-protective.
Other unspecified part is prior art.
Claims (1)
1. HFCS triple effect evaporator, it is characterized in that it comprises the first evaporimeter (3), the second evaporimeter (4), the 3rd evaporimeter (5), material pot (1), air pump (6), cooling tower (7), vavuum pump (8), finished pot (9);
Described each evaporimeter includes a reboiler and a vaporization chamber, and the bottom of described reboiler is connected with described vaporization chamber;
The import of described air pump (6) is connected with steam inlet tube, outlet is connected with the first evaporimeter reboiler (3a), the overhead vapor outlet of the first vaporization chamber (3b) is connected with the second reboiler (4a), the overhead vapor outlet of the second vaporization chamber (4b) is connected with the 3rd reboiler (5a), the overhead vapor outlet of the 3rd vaporization chamber (5b) is connected with cooling tower (7), and the another side of cooling tower is connected with vavuum pump (8);
The import of described material pot (1) is connected with material inlet pipe, outlet is connected with the first product pump (2a), the outlet of described the first product pump (2a) is connected with the top of the 3rd reboiler (5a), the bottom of the 3rd reboiler (5a) is connected with the bottom of the 3rd vaporization chamber (5b) and leads to the second product pump (2b), the outlet of described the second product pump (2b) is connected with the top of the first reboiler (3a), the bottom of described the first reboiler (3a) is connected and leads to 3 material pump (2c) with the bottom of the first vaporization chamber (3b), the outlet of described 3 material pump (2c) is connected with the top of the second reboiler (4a), the bottom of the second reboiler (4a) is connected and leads to 4 materials pump (2d) with the bottom of the second vaporization chamber (4b), finished pot (9) is led in the outlet of described 4 materials pump (2d).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320750501.2U CN203598508U (en) | 2013-11-25 | 2013-11-25 | High fructose syrup triple-effect concentration evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320750501.2U CN203598508U (en) | 2013-11-25 | 2013-11-25 | High fructose syrup triple-effect concentration evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203598508U true CN203598508U (en) | 2014-05-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320750501.2U Expired - Fee Related CN203598508U (en) | 2013-11-25 | 2013-11-25 | High fructose syrup triple-effect concentration evaporator |
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| CN (1) | CN203598508U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104258585A (en) * | 2014-07-31 | 2015-01-07 | 中国平煤神马集团开封兴化精细化工有限公司 | Triple-effect concentration method for neutralization solution in saccharin production |
-
2013
- 2013-11-25 CN CN201320750501.2U patent/CN203598508U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104258585A (en) * | 2014-07-31 | 2015-01-07 | 中国平煤神马集团开封兴化精细化工有限公司 | Triple-effect concentration method for neutralization solution in saccharin production |
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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: 20140521 Termination date: 20201125 |
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| CF01 | Termination of patent right due to non-payment of annual fee |