CN204824813U - Vegetable oil production system - Google Patents
Vegetable oil production system Download PDFInfo
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- CN204824813U CN204824813U CN201520575456.0U CN201520575456U CN204824813U CN 204824813 U CN204824813 U CN 204824813U CN 201520575456 U CN201520575456 U CN 201520575456U CN 204824813 U CN204824813 U CN 204824813U
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Abstract
The utility model discloses a vegetable oil production system, including reation kettle, a dewatering device, first heat exchanger, the 2nd dewatering device and the finished product jar that links to each other in order, wherein: be equipped with the heating plate in the reation kettle, the heating plate links to each other with outside steam device, the refrigerant import and the refrigerant outlet of first heat exchanger link to each other with a dewatering device's export and the 2nd dewatering device's import respectively, the heat medium import and the heat medium export of first heat exchanger link to each other with outside steam device, still be equipped with a filter unit between the 2nd dewatering device's export and the finished product jar. The utility model provides the high purity of vegetable oil, extensive applicability.
Description
Technical field
The utility model relates to a kind of vegetable oil production system, belongs to vegetables oil special product technical field.
Background technology
Existing vegetable oil production system great majority are made up of associated components such as charging device, reactor, dewatering units, substantially can meet the production of general vegetables oil.But its shortcoming existed is: this vegetable oil production system is to plant oil handling imperfection, and the purity of vegetables oil is not high, affects the use of vegetables oil.
Utility model content
The deficiency that the utility model exists to overcome prior art, provides a kind of vegetable oil production system that can improve vegetable oil purity.
The utility model is achieved by taking following technical scheme:
A kind of vegetable oil production system, comprise the reactor, the first dewatering unit, First Heat Exchanger, the second dewatering unit and the finished pot that are connected in turn, wherein: in described reactor, be provided with heating plate, described heating plate is connected with External steam units, the refrigerant import of described First Heat Exchanger is connected with the outlet of the first dewatering unit and the import of the second dewatering unit respectively with refrigerant exit, the Heating medium of described First Heat Exchanger is connected with External steam units with heating agent outlet, is also provided with a filtering unit between the outlet of described second dewatering unit and finished pot.
Preferably, the top of described reactor and bottom are respectively equipped with opening for feed and discharge port, and described opening for feed place is provided with a charging device.
Preferably, described charging device is charging tank.
Preferably, described first dewatering unit comprises the first dehydration tower and the second interchanger, the first sparger is provided with in described first dehydration tower, its top and bottom are equipped with outlet, described first sparger is connected with the discharge port of reactor, the outlet at the top of described first dehydration tower is connected with the Heating medium of the second interchanger, outlet bottom it is connected with the refrigerant import of First Heat Exchanger, the refrigerant import of described second interchanger is connected with exterior cooling device with refrigerant exit, and the heating agent outlet of described second interchanger is connected with outside waste oil pool.
Preferably, described second dewatering unit comprises the second dehydration tower and the 3rd interchanger, the second sparger is provided with in described second dehydration tower, its top and bottom are equipped with outlet, described second sparger is connected with the refrigerant exit of First Heat Exchanger, the outlet at the top of described second dehydration tower is connected with the Heating medium of the 3rd interchanger, outlet bottom it is connected with the import of strainer, the refrigerant import of described 3rd interchanger is connected with exterior cooling device with refrigerant exit, and the heating agent outlet of described 3rd interchanger is connected with outside waste oil pool.
Preferably, described vegetable oil production system also comprises the 4th interchanger and return tank, the Heating medium of described 4th interchanger is connected with the outlet at the top of reactor, the outlet of its heating agent is connected with the import of return tank, the outlet of described return tank is connected with the import at the top of reactor, and the refrigerant import of described 4th interchanger is connected with exterior cooling device with refrigerant exit.
Preferably, described filtering unit comprises filter.
Preferably, described production system also comprises the connected pipeline and lift pump of being located at each equipment room.
Compared with prior art, the beneficial effects of the utility model are: the utility model is by charging device, reactor, first dewatering unit, First Heat Exchanger, second dewatering unit, filter is connected with outlet successively with the import of finished pot, raw material is made to be transported to finished pot after being filtered by filter after the second dewatering unit carries out processed after First Heat Exchanger heating after the first dewatering unit carries out preliminary hydro-extraction after completing epoxidation reaction in reactor again, obtain high-purity oil plant, realize the production line balance of vegetables oil, simultaneously, improve the purity of vegetables oil, suitability is wide.
Accompanying drawing explanation
Fig. 1 is the structural representation of vegetable oil production system of the present utility model.
Embodiment
Below in conjunction with accompanying drawing, most preferred embodiment of the present utility model is described in detail.
As shown in Figure 1, the vegetable oil production system of the present embodiment comprises the charging device 1 be connected successively, reactor 2, first dewatering unit 3, First Heat Exchanger 4, second dewatering unit 5, filter 6 and finished pot 7 and be connected pipeline and the lift pump of being located at each equipment room, described charging device 1 is charging tank, in described reactor, 2 are provided with heating plate 21, its top has opening for feed, discharge port is had bottom it, described charging device 1 is connected with the opening for feed of reactor 2, described heating plate 21 is connected with External steam units, the import of described first dewatering unit 3 is connected with the discharge port of reactor 2, the refrigerant import of described First Heat Exchanger 4 is connected with the outlet of the first dewatering unit 3, its Heating medium is connected with External steam units with heating agent outlet, the import of described second dewatering unit 5 is connected with the refrigerant exit of First Heat Exchanger 4, the outlet of described second dewatering unit 5 is connected with finished pot 7, between the outlet that described filter 6 is arranged on the second dewatering unit 5 and finished pot 7.Raw material delivers in reactor 2 through the opening for feed of reactor 2 by charging device 1, raw material obtains work in-process vegetables oil carry out polynary carburizing reagent in the heating plate 21 of reactor 2 after, this work in-process vegetables oil flows through the first dewatering unit 3 from the discharge port of reactor 2 and carries out preliminary hydro-extraction process, and this work in-process vegetables oil flows through the second dewatering unit 5 again after First Heat Exchanger 4 heats to carry out concentration processed and deliver to and obtain finished product vegetable oil after strainer 6 carries out contaminant filter and be stored in finished pot 7.
In the present embodiment, described first dewatering unit 3 comprises the first dehydration tower 31 and the second interchanger 32, the first sparger 33 is provided with in described first dehydration tower 31, its top and bottom are equipped with outlet, described first sparger 33 is connected with the discharge port of reactor 2, the outlet at the top of described first dehydration tower 31 is connected with the Heating medium of the second interchanger 32, outlet bottom it is connected with the refrigerant import of First Heat Exchanger 4, the refrigerant import of described second interchanger 32 is connected with exterior cooling device with refrigerant exit, the heating agent outlet of described second interchanger 32 is connected with outside waste oil pool, described second dewatering unit 5 comprises the second dehydration tower 51 and the 3rd interchanger 52, the second sparger 53 is provided with in described second dehydration tower 51, its top and bottom are equipped with outlet, described second sparger 53 is connected with the refrigerant exit of First Heat Exchanger 4, the outlet at the top of described second dehydration tower 51 is connected with the Heating medium of the 3rd interchanger 52, outlet bottom it is connected with the import of strainer 6, the refrigerant import of described 3rd interchanger 52 is connected with exterior cooling device with refrigerant exit, the heating agent outlet of described 3rd interchanger 52 is connected with outside waste oil pool.The first sparger 33 that work in-process vegetables oil flow into the first dehydration tower 31 from the discharge port of the bottom of reactor 2 carries out sorting, part poor quality oil flows to waste oil pool after the second interchanger 32 cools, the outlet flow of remainder vegetables oil through the bottom of the first dehydration tower 31 is to First Heat Exchanger 4, the second sparger 53 that this Activities of Some Plants oil flows to the second dehydration tower 51 after First Heat Exchanger 4 heats carries out sorting, part poor quality oil flows to waste oil pool after the 3rd interchanger 52 cools, the remaining outlet flow of vegetables oil through the bottom of the second dehydration tower 51 is filtered to strainer 6.
In the present embodiment, this vegetable oil production system also comprises the 4th interchanger 8 and return tank 9, the Heating medium of described 4th interchanger 8 is connected with the outlet at the top of reactor 2, the outlet of its heating agent is connected with the import of return tank 9, the outlet of described return tank 9 is connected with the import at the top of reactor 2, the refrigerant import of described 4th interchanger 8 is connected with exterior cooling device with refrigerant exit, flow in return tank 9 after the outlet flow of Activities of Some Plants oil through the top of reactor 2 after heating plate 21 heats cools to the 4th interchanger 8, be back in reactor 2 after this Activities of Some Plants oil dewaters in return tank 9 and enter next step handling procedure.
Claims (8)
1. a vegetable oil production system, it is characterized in that: comprise the reactor be connected in turn, first dewatering unit, First Heat Exchanger, second dewatering unit and finished pot, wherein: in described reactor, be provided with heating plate, described heating plate is connected with External steam units, the refrigerant import of described First Heat Exchanger is connected with the outlet of the first dewatering unit and the import of the second dewatering unit respectively with refrigerant exit, the Heating medium of described First Heat Exchanger is connected with External steam units with heating agent outlet, a filtering unit is also provided with between the outlet of described second dewatering unit and finished pot.
2. vegetable oil production system according to claim 1, is characterized in that: the top of described reactor and bottom are respectively equipped with opening for feed and discharge port, and described opening for feed place is provided with a charging device.
3. vegetable oil production system according to claim 2, is characterized in that: described charging device is charging tank:
4. vegetable oil production system according to claim 1, it is characterized in that described first dewatering unit comprises the first dehydration tower and the second interchanger, the first sparger is provided with in described first dehydration tower, its top and bottom are equipped with outlet, described first sparger is connected with the discharge port of reactor, the outlet at the top of described first dehydration tower is connected with the Heating medium of the second interchanger, outlet bottom it is connected with the refrigerant import of First Heat Exchanger, the refrigerant import of described second interchanger is connected with exterior cooling device with refrigerant exit, the heating agent outlet of described second interchanger is connected with outside waste oil pool.
5. vegetable oil production system according to claim 1, it is characterized in that described second dewatering unit comprises the second dehydration tower and the 3rd interchanger, the second sparger is provided with in described second dehydration tower, its top and bottom are equipped with outlet, described second sparger is connected with the refrigerant exit of First Heat Exchanger, the outlet at the top of described second dehydration tower is connected with the Heating medium of the 3rd interchanger, outlet bottom it is connected with the import of strainer, the refrigerant import of described 3rd interchanger is connected with exterior cooling device with refrigerant exit, the heating agent outlet of described 3rd interchanger is connected with outside waste oil pool.
6. vegetable oil production system according to any one of claim 1 to 5, characterized by further comprising the 4th interchanger and return tank, the Heating medium of described 4th interchanger is connected with the outlet at the top of reactor, the outlet of its heating agent is connected with the import of return tank, the outlet of described return tank is connected with the import at the top of reactor, and the refrigerant import of described 4th interchanger is connected with exterior cooling device with refrigerant exit.
7. vegetable oil production system according to any one of claim 1 to 5, is characterized in that: described filtering unit comprises filter.
8. vegetable oil production system according to any one of claim 1 to 5, is characterized in that: described production system also comprises the connected pipeline and lift pump of being located at each equipment room.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520575456.0U CN204824813U (en) | 2015-07-31 | 2015-07-31 | Vegetable oil production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520575456.0U CN204824813U (en) | 2015-07-31 | 2015-07-31 | Vegetable oil production system |
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| Publication Number | Publication Date |
|---|---|
| CN204824813U true CN204824813U (en) | 2015-12-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520575456.0U Active CN204824813U (en) | 2015-07-31 | 2015-07-31 | Vegetable oil production system |
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| Country | Link |
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| CN (1) | CN204824813U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106318621A (en) * | 2016-08-26 | 2017-01-11 | 南通海珥玛科技股份有限公司 | Equipment special for vegetable oil deacidification and deodorization and vegetable oil deacidification and deodorization technology |
-
2015
- 2015-07-31 CN CN201520575456.0U patent/CN204824813U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106318621A (en) * | 2016-08-26 | 2017-01-11 | 南通海珥玛科技股份有限公司 | Equipment special for vegetable oil deacidification and deodorization and vegetable oil deacidification and deodorization technology |
| CN106318621B (en) * | 2016-08-26 | 2019-09-24 | 南通海珥玛科技股份有限公司 | One vegetable oil deacid-deodoring special equipment and vegetable oil deacid-deodoring technique |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Vegetable oil production system Effective date of registration: 20170720 Granted publication date: 20151202 Pledgee: Guangzhou Caold financing Company limited by guarantee Pledgor: Hairma Chemicals (GZ) Ltd. Registration number: 2017440000054 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20180212 Granted publication date: 20151202 Pledgee: Guangzhou Caold financing Company limited by guarantee Pledgor: Hairma Chemicals (GZ) Ltd. Registration number: 2017440000054 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Vegetable oil production system Effective date of registration: 20180227 Granted publication date: 20151202 Pledgee: Guangzhou Caold financing Company limited by guarantee Pledgor: Hairma Chemicals (GZ) Ltd. Registration number: 2018440000042 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20190304 Granted publication date: 20151202 Pledgee: Guangzhou Caold financing Company limited by guarantee Pledgor: Hairma Chemicals (GZ) Ltd. Registration number: 2018440000042 |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190307 Address after: 226017 No. 1 Tongshun Road, Nantong Development Zone, Nantong City, Jiangsu Province Patentee after: NANTONG HAIERMA TECHNOLOGY CO., LTD. Address before: 510000 New Yagang Village, Shijingjie Street, Baiyun District, Guangzhou City, Guangdong Province, No. 1 Patentee before: Hairma Chemicals (GZ) Ltd. |