CN203065435U - Complete equipment for extracting fish oil from fish meal - Google Patents
Complete equipment for extracting fish oil from fish meal Download PDFInfo
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- CN203065435U CN203065435U CN 201320067854 CN201320067854U CN203065435U CN 203065435 U CN203065435 U CN 203065435U CN 201320067854 CN201320067854 CN 201320067854 CN 201320067854 U CN201320067854 U CN 201320067854U CN 203065435 U CN203065435 U CN 203065435U
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Abstract
The utility model relates to complete equipment for extracting fish oil from fish meal, which can effectively solve the problems that as the content of fish oil in fish meal is excessively high, the fish meal is easy to degrade and go bad, and the protein content is low. The complete equipment is structurally characterized in that a quantitative feeding device is communicated with an elevator, the elevator is communicated with an auger through a conditioner, a forming machine, a belt conveyor, a low-temperature drying device, a scraper plate and a storage box which are connected in series, the auger is communicated with an extractor, an outlet of the extractor is communicated with an inlet of a low-temperature desolventizing device through the scraper plate and the auger, another outlet of the extractor is communicated with the inlet of a first-effect long tube evaporator through a pump, a separator, a filter and a mixed oil tank which are connected in series, the outlet of the first-effect long tube evaporator is communicated with the inlet of a flash evaporation tank, the outlet of the flash evaporation tank is communicated with the inlet of a fish oil storage tank sequentially through a second-effect long tube evaporator, the flash evaporation tank, a third-effect falling-film evaporator, the pump for pumping a solvent and a concentration tank which are connected in series, and a third outlet of the extractor is communicated with a condenser. The complete equipment is convenient to install and use and has a good effect; and fish meal products have high quality and are not easy to go bad.
Description
Technical field
The utility model relates to chemical industry equipment, particularly utilizes a kind of suite of equipment that extracts fish oil from fish meal of low-temperature extraction technology.
Technical background
Fish meal is as the main raw material of fodder industry, and protein content is more high more good. and generally about 1.2%, protein content is about 70% for the fish oil amount that contains of preceding external high-grade fish meal.Domestic for reducing the fish oil content in the fish meal, adopt twice pressing technology.Fish oil content is about 15% in the fish meal before the squeezing, and the fish oil content of squeezing back fish meal is generally at 8--9 %, and protein content is about 64%.Well below foreign standard, because fish oil content is higher, easily deterioration is rotten, and protein content is low, particularly in summer, domestic fish meal difficulty is deposited, but squeezing process itself has determined can not be clean with the squeezing of the fish oil in the fish meal, corresponding support equipment must be arranged, but the equipment that uses at present is because structural problem, its use is unsatisfactory, yet there are no any being applicable to and utilizes the low-temperature extraction technology to extract the report of the suite of equipment of fish oil from fish meal.
Summary of the invention
At above-mentioned situation, for overcoming the defective of prior art, the purpose of the utility model just provides a kind of suite of equipment that extracts fish oil from fish meal, can effectively solve fish oil too high levels in the fish meal, and easily deterioration is rotten, the problem that protein content is low.
The technical scheme that the utility model solves is, this equipment comprises quantitative feeder, lift, shaper and rotary conveyor, quantitatively the feeder discharge port is connected with the first lift opening for feed, the first lift opening for feed is the quality-adjusting device through connecting successively, second lift, shaper, rotary conveyor, the oven drying at low temperature device, bury scraper plate, the flat scraper plate of carrying, the first bent scraper plate, buffer bin is connected with the opening for feed of the first sealing auger, the discharge port of the first sealing auger is connected with the opening for feed of multi-stage counter current extraction device, three outlets are arranged on the multi-stage counter current extraction device, an outlet is through the second bent scraper plate, the second sealing auger is connected with the material inlet of low temperature desolventizing device, the material outlet of low temperature desolventizing device is connected with the scraper plate import through solvent trap, the fish meal storage tank is housed on the low temperature desolventizing device, another outlet of multi-stage counter current extraction device is first pump that is used for taking out solvent through connecting successively, wet cyclone, accurate filter, miscella tank and one is imitated the long-tube evaportor import and is connected, one outlet of imitating long-tube evaportor is connected with the import of No. 1 shwoot case, the outlet of No. 1 shwoot case is imitated long-tube evaportor through two of series connection successively, No. 2 shwoot casees, the triple effect falling-film evaporator, No. 3 shwoot casees, be used for taking out second pump of solvent, concentration tank is connected with the import of fish oil storage tank, and the 3rd outlet of multi-stage counter current extraction device is connected with the import of first condenser.
The utility model novel structure uniqueness, easy to install, effective, the product fish oil content of producing is low, good product quality, not perishable, economic worth is big.
Description of drawings
Fig. 1 is structural frames diagram of the present utility model.
Embodiment
Below in conjunction with accompanying drawing embodiment of the present utility model is elaborated.
By shown in Figure 1, the utility model comprises quantitative feeder, lift, shaper and rotary conveyor, quantitatively feeder 1 discharge port is connected with first lift, 2 opening for feeds, first lift, 2 opening for feeds are the quality-adjusting device 3 through connecting successively, second lift 4, shaper 5, rotary conveyor 6, oven drying at low temperature device 7, bury scraper plate 8, the flat scraper plate 9 of carrying, the first bent scraper plate 10, buffer bin 11 is connected with the opening for feed of the first sealing auger 12, the discharge port of the first sealing auger 12 is connected with the opening for feed of multi-stage counter current extraction device 13, three outlets are arranged on the multi-stage counter current extraction device 13, an outlet is through the second bent scraper plate 14, the second sealing auger 15 is connected with the material inlet of low temperature desolventizing device 16, the material outlet of low temperature desolventizing device 16 is connected with scraper plate 19 imports through solvent trap 18, fish meal storage tank 17 is housed on the low temperature desolventizing device 16, another outlet of multi-stage counter current extraction device 13 is first pump 22 that is used for taking out solvent through connecting successively, wet cyclone 23, accurate filter 24, miscella tank 25 and one is imitated long-tube evaportor 26 imports and is connected, one outlet of imitating long-tube evaportor 26 is connected with No. 1 shwoot case 27 imports, the outlet of No. 1 shwoot case 27 is imitated long-tube evaportor 28 through two of series connection successively, No. 2 shwoot casees 31, triple effect falling-film evaporator 32, No. 3 shwoot casees 33, be used for taking out second pump 34 of solvent, concentration tank 35 is connected with the import of fish oil storage tank 36, and the 3rd outlet of multi-stage counter current extraction device 13 is connected with the import of first condenser 39.
In order to guarantee result of use and to take full advantage of raw material, economize on resources, the outlet of described scraper plate 19 is connected with 13 imports of multi-stage counter current extraction device through the big sprayed tank 38 of the 3rd pump 37, solvent of series connection with the import that connects integrated water branch mailbox 20 after the outlet of first condenser 39, second condenser 45 is in parallel, the outlet of integrated water branch mailbox 20;
The import of described integrated water branch mailbox 20 is connected with the outlet of the 3rd condenser 29, water cycle vacuum pump 30, the three condensers 29 is housed on the 3rd condenser 29 is connected with No. 2 shwoot casees 31, No. 3 shwoot casees 33, concentration tanks 35 of parallel connection;
Described scraper plate 19 links to each other with tail gas condenser 21, tail gas condenser 21 links to each other with absorption tower 40, second condenser 45 respectively, the outlet on absorption tower 40 links to each other with the import of water cooler 46 through the 4th pump 42, the 5th pump 43, the Analytic Tower 44 of series connection, the outlet of water cooler 46 links to each other with the import on absorption tower 40, the outlet of Analytic Tower 44 links to each other with 45 imports of second condenser, and the blower fan 41 of discharging tail gas is housed on the absorption tower 40.
By said structure as can be seen, each parts of the utility model are made of integrated through scientific and reasonable combination pipeline, be suitable for industrialized mass production, make that fish oil content is lower than 1% in the fish meal, efficiently solve fish oil too high levels in the fish meal, easily deterioration is rotten, the problem that protein content is low.Because the market price of fish oil is higher than fish meal far away, has increased the added value of fish meal, is that one on the fish meal processing units innovated greatly, economic and social benefit is huge.
Claims (4)
- One kind from fish meal the extraction fish oil suite of equipment, comprise quantitative feeder, lift, shaper and rotary conveyor, it is characterized in that, quantitatively feeder (1) discharge port is connected with first lift (2) opening for feed, first lift (2) opening for feed is the quality-adjusting device (3) through connecting successively, second lift (4), shaper (5), rotary conveyor (6), oven drying at low temperature device (7), bury scraper plate (8), the flat scraper plate (9) of carrying, the first bent scraper plate (10), buffer bin (11) is connected with the opening for feed of the first sealing auger (12), the discharge port of the first sealing auger (12) is connected with the opening for feed of multi-stage counter current extraction device (13), three outlets are arranged on the multi-stage counter current extraction device (13), an outlet is through the second bent scraper plate (14), the second sealing auger (15) is connected with the material inlet of low temperature desolventizing device (16), the material outlet of low temperature desolventizing device (16) is connected through the same scraper plate of solvent trap (18) (19) import, fish meal storage tank (17) is housed on the low temperature desolventizing device (16), another outlet of multi-stage counter current extraction device (13) is first pump (22) that is used for taking out solvent through connecting successively, wet cyclone (23), accurate filter (24), miscella tank (25) and one is imitated long-tube evaportor (26) import and is connected, one outlet of imitating long-tube evaportor (26) is connected with No. 1 shwoot case (27) import, the outlet of No. 1 shwoot case (27) is imitated long-tube evaportor (28) through two of series connection successively, No. 2 shwoot casees (31), triple effect falling-film evaporator (32), No. 3 shwoot casees (33), be used for taking out second pump (34) of solvent, concentration tank (35) is connected with the import of fish oil storage tank (36), and the 3rd outlet of multi-stage counter current extraction device (13) is connected with the import of first condenser (39).
- According to claim 1 from fish meal the extraction fish oil suite of equipment, it is characterized in that, the outlet of described scraper plate (19) is connected with multi-stage counter current extraction device (13) import through the 3rd pump (37), the big sprayed tank of solvent (38) of series connection with the import that connects integrated water branch mailbox (20) after the outlet of first condenser (39), second condenser (45) is in parallel, the outlet of integrated water branch mailbox (20).
- According to claim 2 from fish meal the extraction fish oil suite of equipment, it is characterized in that, the import of described integrated water branch mailbox (20) is connected with the outlet of the 3rd condenser (29), water cycle vacuum pump (30) is housed on the 3rd condenser (29), and the 3rd condenser (29) is connected with No. 2 shwoot casees (31), No. 3 shwoot casees (33), the concentration tank (35) of parallel connection.
- According to claim 1 from fish meal the extraction fish oil suite of equipment, it is characterized in that, described scraper plate (19) links to each other with tail gas condenser (21), tail gas condenser (21) respectively with absorption tower (40), second condenser (45) links to each other, the outlet on absorption tower (40) is through the 4th pump (42) of series connection, the 5th pump (43), Analytic Tower (44) links to each other with the import of water cooler (46), the outlet of water cooler (46) links to each other with the import of absorption tower (40), the outlet of Analytic Tower (44) links to each other with second condenser (45) import, and the blower fan (41) of discharging tail gas is housed on absorption tower (40).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN 201320067854 CN203065435U (en) | 2013-02-06 | 2013-02-06 | Complete equipment for extracting fish oil from fish meal |
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CN 201320067854 CN203065435U (en) | 2013-02-06 | 2013-02-06 | Complete equipment for extracting fish oil from fish meal |
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CN203065435U true CN203065435U (en) | 2013-07-17 |
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CN 201320067854 Expired - Lifetime CN203065435U (en) | 2013-02-06 | 2013-02-06 | Complete equipment for extracting fish oil from fish meal |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103820220A (en) * | 2014-03-20 | 2014-05-28 | 河南华泰粮油机械工程有限公司 | Method for simultaneously continuous stable production of soybean leached wet meal through two different production lines of high-temperature desolvation and low-temperature desolvation |
CN104651032A (en) * | 2014-12-26 | 2015-05-27 | 化州市新海水产有限公司 | Fish oil extracting device |
CN105154236A (en) * | 2015-09-23 | 2015-12-16 | 陈富强 | Full-automatic electric heating triple-effect plant essential oil extracting and purifying integrated device |
CN107667996A (en) * | 2017-11-06 | 2018-02-09 | 扬州中欧工业机器人有限公司 | Fish capture categorizing system automatically |
-
2013
- 2013-02-06 CN CN 201320067854 patent/CN203065435U/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103820220A (en) * | 2014-03-20 | 2014-05-28 | 河南华泰粮油机械工程有限公司 | Method for simultaneously continuous stable production of soybean leached wet meal through two different production lines of high-temperature desolvation and low-temperature desolvation |
CN104651032A (en) * | 2014-12-26 | 2015-05-27 | 化州市新海水产有限公司 | Fish oil extracting device |
CN105154236A (en) * | 2015-09-23 | 2015-12-16 | 陈富强 | Full-automatic electric heating triple-effect plant essential oil extracting and purifying integrated device |
CN107667996A (en) * | 2017-11-06 | 2018-02-09 | 扬州中欧工业机器人有限公司 | Fish capture categorizing system automatically |
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Granted publication date: 20130717 |
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CX01 | Expiry of patent term |