CN202605758U - Distilling device for ethyl maltol - Google Patents
Distilling device for ethyl maltol Download PDFInfo
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- CN202605758U CN202605758U CN 201220267743 CN201220267743U CN202605758U CN 202605758 U CN202605758 U CN 202605758U CN 201220267743 CN201220267743 CN 201220267743 CN 201220267743 U CN201220267743 U CN 201220267743U CN 202605758 U CN202605758 U CN 202605758U
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- still
- ethyl maltol
- distilling
- distillation still
- loading hopper
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Abstract
The utility model discloses a distilling device for ethyl maltol. The distilling device comprises a distilling kettle, a feeding hopper, a receiving kettle and a heating component, wherein the distilling kettle is used for distilling crude ethyl maltol products to form a gaseous substance containing the ethyl maltol; the feeding hopper is used for supplying the crude ethyl maltol products to the distilling kettle and connected with the distilling kettle; the receiving kettle is used for retreating the gaseous substance and connected with the distilling kettle; and the heating component is used for supplying heat to the distilling kettle and connected with the distilling kettle. The distilling device has the advantages that the crude ethyl maltol products are supplied to the distilling kettle through the feeding hopper, so that the crude ethyl maltol products can be continuously fed into the distilling kettle and continuously distilled by the distilling kettle, and the production efficiency is high; the distilling kettle is not required to be supplied with a large number of crude ethyl maltol products at one time, so that a stirring motor is not required, and the cost is low; and simultaneously, the crude ethyl maltol products can be fully distilled, a few residues are generated, and the distilling device is environment-friendly.
Description
Technical field
The utility model relates to a kind of distilling apparatus of ethyl maltol.
Background technology
The solid distillation of spices is to adopt direct-fired method in industry always, and at first heating makes the solid dissolving, and then the distillation of rising temperature.The shortcoming of this distillation is that heat is transmitted to inside by the outside through solid again, has caused heat time heating time long owing to be external heat; And spices is stable poor; In long heating process, can produce polymerization, the fragrance of fragrance material is changed.
Existing production technology to ethyl maltol is: the ethyl maltol coarse fodder obtains yellow thin shape material through coarse crystallization; According to distillation crystallization kettle size (also have be called distillation crystallization) the yellow filamentary material 200-300KG of disposable throwing; Heat through chuck heat conduction oil bath; Solid material progressively is warmed up to more than 90 ℃ and begins the fusion that distils in the still; Vacuumize, still is accepted in the ethyl maltol suction, make water absorb the material that distills; High boiling polymer is then stayed in the distillation crystallization kettle, forms pitch shape residue and discharges; In temperature-rise period, whenever stir for several times, to prevent tying on the still wall service life of reduction distillation crystallization kettle after the solid conductive heat inequality from making hot-spot cause the material carbonization at a distance from 5-10 minute needs crawl.Therefore, this distilling apparatus adopts disposable feeding intake, because the granular solids poor thermal conductivity, not only still-process is very long and production efficiency is low; Simultaneously, also need frequent crawl to stir, make that the motor load that stirs is big, service life is short; And level of residue is unfavorable for environmental protection greatly, and the rate of recovery is low-cost high.
The utility model content
The utility model provides a kind of distilling apparatus of ethyl maltol, and it has overcome the existing deficiency of background technology.The technical scheme that is adopted that the utility model solves its technical problem is: a kind of distilling apparatus of ethyl maltol, and it comprises:
One is used for the ethyl maltol bullion is distilled the distillation still (100) that forms the gaseous matter that contains ethyl maltol;
One is used for supplying with to distillation still (100) loading hopper (200) of ethyl maltol bullion, and it connects said distillation still (100);
One is used for accepting still to what gaseous matter was handled again, and it connects said distillation still (100); And
One is used for the heating component to distillation still (100) feed heat, and it connects said distillation still (100).
Among one preferred embodiment: also be provided with a pneumatic operated valve (10) between said loading hopper (200) and the distillation still (100).
Among one preferred embodiment: said loading hopper (200) connects said heating component respectively and accepts still.
Among one preferred embodiment: said accept also to be provided with between still and the distillation still (100) one be used for the gaseous matter suction is accepted still vavuum pump.
Among one preferred embodiment: the heat that said heating component provides is a steam.
Among one preferred embodiment: between said distillation still (100) and the loading hopper (200), between said distillation still (100) and the heating component, said distillation still (100) with accept between the still, saidly accept between still and the loading hopper (200) and all be connected between said loading hopper (200) and the heating component through pipeline; And the pipeline between said distillation still (100) and the heating component is provided with a control valve (20); Said distillation still (100) and the pipeline of accepting between the still are provided with a control valve (30); The said pipeline of accepting between still and the loading hopper (200) is provided with a control valve (40), and the pipeline between said loading hopper (200) and the heating component is provided with a control valve (50).
The present technique scheme is compared with background technology, and it has following advantage:
1. supply with the ethyl maltol bullion through a loading hopper to distillation still, can feed in raw material to distillation still continuously and then make distillation still carry out continuous still, the production efficiency height; And do not need disposable a large amount of feed of distillation still to be avoided the use of stirring motor, reduce cost; Simultaneously; The ethyl maltol bullion can fully distill, and level of residue is little, environmental protection.
2. be provided with pneumatic operated valve between loading hopper and the distillation still, make and to carry out feed from the trend distillation still, not only enhance productivity, and practice thrift cost of labor.
3. loading hopper connects said heating component respectively and accepts still; Make the bullion in loading hopper be heated the liquid supply of back formation, shorten and distill flow process, raise the efficiency to distillation still; The rate of recovery of ethyl maltol is increased; Cost reduces, and in loading hopper, also can distill and gaseous matter flowed to and accept still, further raises the efficiency.
4. the heat that provides of heating component is a steam, cuts down the consumption of energy.
5. each pipeline is equipped with control valve, can carry out management and control to each link at any time, easy to operate, safety.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the utility model is described further.
Fig. 1 has illustrated the overall schematic of distilling apparatus of a kind of ethyl maltol of a preferred embodiment.
The specific embodiment
Please refer to Fig. 1, an a kind of preferred embodiment of distilling apparatus of ethyl maltol, the distilling apparatus of described a kind of ethyl maltol, it comprises: a distillation still 100, a loading hopper 200, are accepted still, a heating component.
Said distillation still 100 is used for the ethyl maltol bullion is distilled the gaseous matter that formation contains ethyl maltol.
Said loading hopper 200 is used for supplying with the ethyl maltol bullion to distillation still 100, and it connects said distillation still 100.Supply with the ethyl maltol bullions through a loading hopper to distillation still 100, can feed in raw material to distillation still 100 continuously and then make distillation still carry out continuous still, the production efficiency height; And do not need disposable distillation still 100 a large amount of feed to be avoided the use of stirring motor, reduce cost; Simultaneously; The ethyl maltol bullion can fully distill, and level of residue is little, environmental protection.In the present embodiment, also be provided with a pneumatic operated valve 10 between said loading hopper 200 and the distillation still 100, make and to carry out feed from the trend distillation still, not only enhance productivity, and practice thrift cost of labor.
The said still of accepting is used for gaseous matter is handled again, and it connects said distillation still 100, and is as shown in Figure 1, and it is positioned at 2 ends.In the present embodiment, said accept also to be provided with between still and the distillation still 100 one be used for the gaseous matter suction is accepted still vavuum pump.
Said heating component is used for to distillation still 100 feed heats, and it connects said distillation still 100, and is as shown in Figure 1, and it is positioned at 1 end.In the present embodiment, the heat that said heating component provides is a steam, cuts down the consumption of energy.
In the present embodiment, said loading hopper 200 connects said heating component respectively and accepts still.Make the bullion in loading hopper be heated the liquid supply of back formation, shorten and distill flow process, raise the efficiency to distillation still; The rate of recovery of ethyl maltol is increased; Cost reduces, and in loading hopper, also can distill and gaseous matter flowed to and accept still, further raises the efficiency.
Best; Between said distillation still 100 and the loading hopper 200, between said distillation still 100 and the heating component, said distillation still 100 with accept between the still, saidly accept between still and the loading hopper 200 and all be connected between said loading hopper 200 and the heating component through pipeline; And the pipeline between said distillation still 100 and the heating component is provided with a control valve 20; Said distillation still 100 and the pipeline of accepting between the still are provided with a control valve 30; The said pipeline of accepting between still and the loading hopper 200 is provided with a control valve 40, and the pipeline between said loading hopper 200 and the heating component is provided with a control valve 50.
This distilling apparatus operating procedure is following:
1. in distillation still 100, add a spot of ethyl maltol bullion, carry out heating for dissolving through heating component.
2. in loading hopper 200, add the ethyl maltol bullion, carry out heating for dissolving through heating component.
3. continue distillation still 100 and loading hopper 200 heated and distill.
4. through pneumatic operated valve, in trend distillation still 100, supply with the liquid (dissolved) of ethyl maltol bullion at set intervals.
5. after the ethyl maltol bullion in the loading hopper 200 uses, through vavuum pump still is accepted in the gaseous matter suction and handled again.
The above; Be merely the utility model preferred embodiment; So can not limit the scope that the utility model is implemented according to this, the equivalence of promptly doing according to the utility model claim and description changes and modifies, and all should still belong in the scope that the utility model contains.
Claims (6)
1. the distilling apparatus of an ethyl maltol, it is characterized in that: it comprises:
One is used for the ethyl maltol bullion is distilled the distillation still (100) that forms the gaseous matter that contains ethyl maltol;
One is used for supplying with to distillation still (100) loading hopper (200) of ethyl maltol bullion, and it connects said distillation still (100);
One is used for accepting still to what gaseous matter was handled again, and it connects said distillation still (100); And
One is used for the heating component to distillation still (100) feed heat, and it connects said distillation still (100).
2. the distilling apparatus of a kind of ethyl maltol according to claim 1 is characterized in that: also be provided with a pneumatic operated valve (10) between said loading hopper (200) and the distillation still (100).
3. the distilling apparatus of a kind of ethyl maltol according to claim 2 is characterized in that: said loading hopper (200) connects said heating component respectively and accepts still.
4. the distilling apparatus of a kind of ethyl maltol according to claim 1 is characterized in that: said accept also to be provided with between still and the distillation still (100) one be used for the gaseous matter suction is accepted still vavuum pump.
5. the distilling apparatus of a kind of ethyl maltol according to claim 1, it is characterized in that: the heat that said heating component provides is a steam.
6. according to the distilling apparatus of claim 1 or 2 or 3 or 4 or 5 described a kind of ethyl maltols; It is characterized in that: between said distillation still (100) and the loading hopper (200), between said distillation still (100) and the heating component, said distillation still (100) with accept between the still, saidly accept between still and the loading hopper (200) and all be connected between said loading hopper (200) and the heating component through pipeline; And the pipeline between said distillation still (100) and the heating component is provided with a control valve (20); Said distillation still (100) and the pipeline of accepting between the still are provided with a control valve (30); The said pipeline of accepting between still and the loading hopper (200) is provided with a control valve (40), and the pipeline between said loading hopper (200) and the heating component is provided with a control valve (50).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220267743 CN202605758U (en) | 2012-06-07 | 2012-06-07 | Distilling device for ethyl maltol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220267743 CN202605758U (en) | 2012-06-07 | 2012-06-07 | Distilling device for ethyl maltol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202605758U true CN202605758U (en) | 2012-12-19 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220267743 Expired - Lifetime CN202605758U (en) | 2012-06-07 | 2012-06-07 | Distilling device for ethyl maltol |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202605758U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109675335A (en) * | 2018-12-12 | 2019-04-26 | 安徽金禾实业股份有限公司 | In a kind of maltol and it is yellow it is thin distil before rough machining method |
| CN109851603A (en) * | 2019-02-26 | 2019-06-07 | 宁夏万香源生物科技有限公司 | A kind of ethyl alcohol can continuous recovery type ethylmaltol preparation system |
-
2012
- 2012-06-07 CN CN 201220267743 patent/CN202605758U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109675335A (en) * | 2018-12-12 | 2019-04-26 | 安徽金禾实业股份有限公司 | In a kind of maltol and it is yellow it is thin distil before rough machining method |
| CN109851603A (en) * | 2019-02-26 | 2019-06-07 | 宁夏万香源生物科技有限公司 | A kind of ethyl alcohol can continuous recovery type ethylmaltol preparation system |
| CN109851603B (en) * | 2019-02-26 | 2024-04-26 | 宁夏万香源生物科技有限公司 | Ethanol can retrieve formula ethyl maltol preparation system in succession |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190412 Address after: 361000 Longmen Lane, Haicang Xinyang Industrial Park, Xiamen City, Fujian Province Patentee after: XIAMEN OMK BIOTECHNOLOGY CO., LTD. Address before: 363000 Wennu Industrial Park, Jiaomei Industrial Comprehensive Development Zone, Longhai City, Zhangzhou City, Fujian Province Patentee before: Longhai Bestally Biotechnology Co., Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20121219 |