CN203333674U - Single crystal rock candy production device - Google Patents
Single crystal rock candy production device Download PDFInfo
- Publication number
- CN203333674U CN203333674U CN2013202491653U CN201320249165U CN203333674U CN 203333674 U CN203333674 U CN 203333674U CN 2013202491653 U CN2013202491653 U CN 2013202491653U CN 201320249165 U CN201320249165 U CN 201320249165U CN 203333674 U CN203333674 U CN 203333674U
- Authority
- CN
- China
- Prior art keywords
- single crystal
- crystallizer
- rock candy
- rock sugar
- crystal rock
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 13
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 title abstract description 15
- 239000013078 crystal Substances 0.000 title abstract description 14
- 238000002425 crystallisation Methods 0.000 claims abstract description 26
- 239000006188 syrup Substances 0.000 claims abstract description 19
- 235000020357 syrup Nutrition 0.000 claims abstract description 19
- 239000012452 mother liquor Substances 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims abstract description 8
- 239000011435 rock Substances 0.000 claims description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 239000010413 mother solution Substances 0.000 claims description 4
- 238000004064 recycling Methods 0.000 claims description 4
- 230000008025 crystallization Effects 0.000 abstract description 6
- 229930006000 Sucrose Natural products 0.000 description 4
- 239000005720 sucrose Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 235000008504 concentrate Nutrition 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Images
Abstract
The utility model discloses a single crystal rock candy production device. The single crystal rock candy production device is provided with a rotary single crystal rock candy crystallizer (1), wherein a syrup inlet (5) is arranged at the top of the rotary single crystal rock candy crystallizer (1), a mother liquor outlet (6) is arranged at the bottom of the rotary single crystal rock candy crystallizer (1), the mother liquor outlet (6) is connected with the bottom of a low-temperature concentration tank (4) through a mother liquor circulation pump (2), a material storage tank (3) is also connected with the bottom of the low-temperature concentration tank (4), a discharge port at the bottom end of the low-temperature concentration tank (4) is connected with the syrup inlet (5) of the rotary single crystal rock candy crystallizer (1), and the top end of the low-temperature concentration tank (4) is connected with a vacuum pump and a condenser. All the parts are connected through hard pipelines. The single crystal rock candy production device disclosed by the utility model adopts one or more low-temperature concentration tanks to maintain an oversaturation coefficient of syrup, single crystal rock candy crystals are crystallized and grown up in the rotary single crystal rock candy crystallizer, the thermal efficiency of the device is improved, and the heat exchange area is not limited; the device adopts a rotary crystallization chamber, so that the circulation of rock candy is improved; the productivity of a single machine is greatly improved; the device completely adopts the hard pipelines for connection, so that the leakage problem is overcome; equipment adopts a diversion shoveling plate for automatic unloading, and the labor intensity of employees is reduced.
Description
Technical field:
The utility model relates to a kind of production unit of monocrystal rock sugar.
Background technology:
Traditional monocrystal rock sugar crystallizer Tc is high, and crystallization time is long, and the conversion decomposition loss of Sucrose is larger, and product color is darker.Mostly adopt and wave tank, only have 30 ° to wave interval, the unit production capacity generally is no more than 2 tons, its heating unit is the plate type heating chamber of waving pot bottom, heat interchanging area is restricted, and waves vacuum pipe, steam-pipe, the material pipe of tank and all will implement to be flexible coupling, and leakage phenomenon is more serious.
Summary of the invention:
The utility model, for the above-mentioned deficiency of prior art, provides a kind of supersaturation coefficient that maintains syrup, greatly reduces the conversion of crystallization time and Sucrose and decomposes the monocrystal rock sugar production unit of rate of loss.
Technical solution of the present utility model is: a kind of monocrystal rock sugar production unit, be provided with rotary type monocrystal rock sugar crystallizer, its top is provided with the syrup entrance, bottom is provided with the mother liquor outlet, the mother liquor outlet is connected with the bottom of cryoconcentration tank by the Recycling Mother Solution pump, material storage tank also is connected with the cryoconcentration pot bottom, the discharge port of cryoconcentration tank bottom is connected with the syrup entrance of rotary type monocrystal rock sugar crystallizer, and the top of cryoconcentration tank is connected with vacuum pump, condenser.
The sidewall of described rotary type monocrystal rock sugar crystallizer is provided with the mouth of charging seed, be provided with the crystallisation chamber of cylinder shape in rotary type monocrystal rock sugar crystallizer, crystallisation chamber drives rotation by reducing motor, the sidewall of crystallisation chamber is provided with hole, crystallization chamber is provided with dividing plate longitudinally, the inwall of crystallisation chamber is provided with the water conservancy diversion flight that pitch angle is 3 °-30 °, at the end face of crystallisation chamber, is provided with door with sugar, and the end face of rotary type monocrystal rock sugar crystallizer is provided with discharge port.
The utility model adopts one or more cryoconcentration tank to maintain the supersaturation coefficient of syrup, and the monocrystal rock sugar crystal is grown up at rotary type monocrystal rock sugar crystallizer intercrystalline, has improved the thermo-efficiency of this device, and heat interchanging area is not limited; This device adopts rotary crystallisation chamber, has improved the cyclicity of rock sugar; The unit production capacity can increase substantially; This device all adopts rigid tubing to connect, and has overcome leakage problem; This equipment adopts water conservancy diversion flight automatic discharging, has reduced practitioner's labour intensity.
The accompanying drawing explanation:
Fig. 1 is structural representation of the present utility model.
The structural representation that Fig. 2 is the utility model rotary type monocrystal rock sugar crystallizer.
The A-A sectional view that Fig. 3 is Fig. 2.
Embodiment:
Further illustrate embodiment of the present utility model below in conjunction with accompanying drawing.
As shown in Figures 1 to 3, a kind of monocrystal rock sugar production unit, be provided with rotary type monocrystal rock sugar crystallizer 1, its top is provided with syrup entrance 5, bottom is provided with mother liquor outlet 6, mother liquor outlet 6 is connected with the bottom of cryoconcentration tank 4 by Recycling Mother Solution pump 2, material storage tank 3 also is connected with cryoconcentration tank 4 bottoms, and the discharge port of cryoconcentration tank 4 bottoms is connected with the syrup entrance 5 of rotary type monocrystal rock sugar crystallizer 1, and the top of cryoconcentration tank 4 is connected with vacuum pump, condenser; Above-mentioned all parts are to connect by rigid tubing.
The sidewall of described rotary type monocrystal rock sugar crystallizer 1 is provided with the mouth 10 of charging seed, be provided with the crystallisation chamber 7 of cylinder shape in rotary type monocrystal rock sugar crystallizer 1, crystallisation chamber 7 drives rotation by reducing motor, the sidewall of crystallisation chamber 7 is provided with hole, be provided with dividing plate 8 longitudinally in crystallisation chamber 7, the inwall of crystallisation chamber 7 is provided with the water conservancy diversion flight 9 that pitch angle is 3 °-30 °, at the end face of crystallisation chamber 7, is provided with door 11 with sugar, and the end face of rotary type monocrystal rock sugar crystallizer 1 is provided with discharge port 12.
Rotary type crystallizer rotary drum rotating speed is 1～15 rev/min, crystallisation chamber is divided into four parts by dividing plate, each compartment is equipped with the mouth of charging seed, all be provided with discharge port, the syrup mother liquor can freely be come in and gone out, the crystallisation chamber inboard is with the water conservancy diversion flight, its oblique angle is 3 °-30 °, when crystallization completes, rotating the monocrystal rock sugar particle with it can flow out through outlet automatically, the concentrated syrup through the cryoconcentration tank, join crystallizer from the syrup entrance, after the crystallization chamber Sucrose is separated out, its supersaturation coefficient reduces, the mother liquor that has reduced supersaturation coefficient flows out from the outlet of syrup mother liquor, return to the cryoconcentration tank.
Claims (2)
1. a monocrystal rock sugar production unit, it is characterized in that: be provided with rotary type monocrystal rock sugar crystallizer (1), its top is provided with syrup entrance (5), bottom is provided with mother liquor outlet (6), mother liquor outlet (6) is connected with the bottom of cryoconcentration tank (4) by Recycling Mother Solution pump (2), material storage tank (3) also is connected with cryoconcentration tank (4) bottom, the discharge port of cryoconcentration tank (4) bottom is connected with the syrup entrance (5) of rotary type monocrystal rock sugar crystallizer (1), and the top of cryoconcentration tank (4) is connected with vacuum pump, condenser; Above-mentioned all parts are to connect by rigid tubing.
2. a kind of monocrystal rock sugar production unit according to claim 1, it is characterized in that: the sidewall of described rotary type monocrystal rock sugar crystallizer (1) is provided with charge seed mouthful (10), be provided with the crystallisation chamber (7) of cylinder shape in rotary type monocrystal rock sugar crystallizer (1), crystallisation chamber (7) drives rotation by reducing motor, the sidewall of crystallisation chamber (7) is provided with hole, be provided with dividing plate (8) longitudinally in crystallisation chamber (7), the inwall of crystallisation chamber (7) is provided with the water conservancy diversion flight (9) that pitch angle is 3 °-30 °, end face in crystallisation chamber (7) is provided with door with sugar (11), the end face of rotary type monocrystal rock sugar crystallizer (1) is provided with discharge port (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202491653U CN203333674U (en) | 2013-05-06 | 2013-05-06 | Single crystal rock candy production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202491653U CN203333674U (en) | 2013-05-06 | 2013-05-06 | Single crystal rock candy production device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203333674U true CN203333674U (en) | 2013-12-11 |
Family
ID=49702360
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013202491653U Expired - Fee Related CN203333674U (en) | 2013-05-06 | 2013-05-06 | Single crystal rock candy production device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203333674U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106566898A (en) * | 2016-10-18 | 2017-04-19 | 孙铁君 | Single-crystal rock candy production equipment |
| CN108686398A (en) * | 2018-07-18 | 2018-10-23 | 浙江优源科技有限公司 | A kind of swinging crystallizer |
| CN112320039A (en) * | 2020-11-10 | 2021-02-05 | 湖南创源生物科技有限公司 | Holding vessel is used to syrup product with partition structure |
-
2013
- 2013-05-06 CN CN2013202491653U patent/CN203333674U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106566898A (en) * | 2016-10-18 | 2017-04-19 | 孙铁君 | Single-crystal rock candy production equipment |
| CN108686398A (en) * | 2018-07-18 | 2018-10-23 | 浙江优源科技有限公司 | A kind of swinging crystallizer |
| CN112320039A (en) * | 2020-11-10 | 2021-02-05 | 湖南创源生物科技有限公司 | Holding vessel is used to syrup product with partition structure |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20151210 Granted publication date: 20131211 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20160610 Granted publication date: 20131211 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20170330 Granted publication date: 20131211 |
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| PD01 | Discharge of preservation of patent | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20220130 Granted publication date: 20131211 |
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| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20220130 Granted publication date: 20131211 |
|
| PD01 | Discharge of preservation of patent | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20230506 Granted publication date: 20131211 |
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| 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: 20131211 |