CN202286145U - Device for recycling liquid protein in fish meal through concentration - Google Patents
Device for recycling liquid protein in fish meal through concentration Download PDFInfo
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- CN202286145U CN202286145U CN2011203729848U CN201120372984U CN202286145U CN 202286145 U CN202286145 U CN 202286145U CN 2011203729848 U CN2011203729848 U CN 2011203729848U CN 201120372984 U CN201120372984 U CN 201120372984U CN 202286145 U CN202286145 U CN 202286145U
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- inspissator
- fish meal
- effect
- liquid protein
- blast pipe
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Abstract
The utility model discloses a device for recycling liquid protein in fish meal through concentration. At present, ideal methods for recycling liquid protein in fish meal do not exist, during recycling, the liquid protein is directly heated, evaporated and concentrated or is treated as dirt, and the two methods are not desirable. The device has the following beneficial effects: a first-effect concentrator heats and concentrates entering liquid protein in fish meal via hot steam generated after drying the fish meal, the heat which is not completely exhausted enters a second-effect concentrator via a steam pipe to heat and concentrate the entering liquid protein in fish meal, the hot steam generated by heating and concentrating the liquid protein in fish meal heats and concentrates the liquid protein in fish meal in a third-effect concentrator via an evaporating hot gas pipe, and the liquid protein undergoing multi-effect concentration can re-enter a drying machine to be dried into the fish meal; and the device takes full advantages of the steam and hot gas generated in fish meal production and does not waste energy, thus achieving the aims of controlling air pollution and protecting the environment.
Description
Technical field
The utility model relates to a kind of fish meal protein liquid concentrating recovery device, belong to field of mechanical technique.
Background technology
First procedure of fish meal production is exactly the processing procedure of low trash fish raw material, and in this process, low trash fish raw material can ooze out partly liquid; Protein and flesh of fish solid content are contained in these liquid the insides, are called protein liquid, and the content of flesh of fish solid content is 4-5% in the protein liquid; If this is the insufficient utilization of protein liquid partly, then can cause great waste, and discarded protein liquid also can destroy environment; Because the protein in the fish meal protein liquid is a kind of very easily corrupt material, the stench perverse nose of gas that after the utmost point will be corrupt in the short time, be corrupt, comes out is unpleasant; In air, float diffusingly lastingly, air has been constituted great pollution.And protein liquid obtains fish meal through behind the concentrate drying, and this has just reduced the fish meal production cost.But to the recycling of these fish meal protein liquid, also not having comparatively ideal way at present, is that direct heating evaporation concentrates during recovery, and the concentrated steam that is produced floats diffusing in air, and another kind of way can only be handled as dirt exactly.These two kinds of methods all are extremely infeasible.In the removal process of protein liquid, should avoid pollution to air ambient to reach again and reclaim thoroughly, thing of difficulty relatively really, so a kind of device of desirable recovery fish meal protein is provided, production is a kind of effective measure of technological progress to fish meal.
Summary of the invention
The purpose of the utility model is a kind of fish meal protein liquid concentrating recovery device of design; Overcome fish meal production process fish meal protein liquid and pass into disuse, and cause the waste and the deficiency of contaminated environment, reclaim fish meal protein liquid through concentrating; Reduce the fish meal production cost, increase benefit.
The realization of above-mentioned purpose; It is because adopted following technical proposals: a kind of fish meal protein liquid concentrating recovery device; Imitating inspissator by one is connected through blast pipe and two effect inspissators; One imitates inspissator is communicated with the triple effect inspissator through elementary blast pipe, vapour liquid separator and secondary blast pipe; Two imitate inspissator also is connected with the triple effect inspissator through elementary blast pipe, vapour liquid separator and secondary blast pipe; The fluid storage compartment that one effect inspissator, two is imitated inspissators and triple effect inspissator is connected through water pipe, and the triple effect inspissator is connected with the triple effect condenser through elementary blast pipe, vapour liquid separator and secondary blast pipe, and vavuum pump is connected with the triple effect condenser through tracheae; Make triple effect condenser, triple effect inspissator; And one imitate the inspissator fluid storage compartment and can both form subnormal ambient with secondary inspissator fluid storage compartment, and two imitate inspissators imitates condensers through blast pipe and two and is connected, blower fan through two imitate condensers tracheae make two to imitate the heat-exchanging chamber of inspissators and the heat-exchanging chamber formation subnormal ambient of an effect inspissator.
Adopt the utility model of above-mentioned measure; One imitates the vapours heating that inspissator produced after through external dry fish meal concentrates the fish meal protein liquid that gets into; The heat that does not run out of gets into two through steam pipe again and imitates the concentrated fish meal protein liquid that gets into of heating in the inspissator; Heating concentrates the vapours that fish meal protein liquid produced and concentrates the fish meal protein liquid in the triple effect inspissator through the heating of heat of evaporation tracheae, and the protein liquid after concentrating through multiple-effect has reached quite high flesh of fish solid content; After concentrating through vacuum, can get in the drying machine dry and become fish meal once more.The utility model has made full use of steam and the hot gas that is produced in the fish meal production, does not waste energy, and also contaminated air has not been recycled the leftover bits and pieces during fish meal is produced, and has reduced the fish meal production cost, has reached the improvement air pollution, the purpose of protection environment.
For specifying the utility model, combine accompanying drawing and embodiment that the utility model is done further to detail below again.
Description of drawings
Accompanying drawing 1 is the structural representation of the utility model;
The specific embodiment
Shown in accompanying drawing 1, the utility model imitates by one that inspissator 1, two is imitated inspissators 2, triple effect inspissator 3, two imitates condensers 4 and triple effect condenser 5 is formed, and above-mentioned parts outward appearance all is drums, all is that above-mentioned parts cut open the structure after showing shown in the accompanying drawing 1.One effect inspissator, 1 bottom is fluid storage compartment 1-1; The middle part is the tubulation 1-2 that communicates with fluid storage compartment 1-1; Space between the tubulation 1-2 is heat-exchanging chamber 1-3; Separate by dividing plate between heat-exchanging chamber 1-3 and the fluid storage compartment 1-1 and do not communicate, separate by dividing plate between heat-exchanging chamber 1-3 and the upper liquid distributor chamber 1-11 and do not communicate.Outside at an effect inspissator 1; Be provided with the air inlet pipe 1-4 that lets vapours get into heat-exchanging chamber 1-3; Be provided with the blast pipe 1-5 that the vapours after the heat exchange is discharged; Protein liquid circulates in tubulation 1-2 through liquid pump 1-10 from top to down among the fluid storage compartment 1-1, in the process of circulation with heat-exchanging chamber 1-3 in vapours carry out heat exchange, evaporation also concentrates gradually.The outside of one effect inspissator 1 also is provided with the elementary blast pipe 1-6 of the hot-air discharge that is produced after the protein liquid heating that communicates with fluid storage compartment 1-1; Elementary blast pipe 1-6 enters hot-air earlier among the vapour liquid separator 1-7; Vapour-liquid obtains separating in vapour liquid separator 1-7; Liquid passes back into fluid storage compartment 1-1, and hot-air enters the heat-exchanging chamber 3-3 of triple effect inspissator through secondary blast pipe 1-8, carries out heat exchange with protein liquid among three grades of inspissator tubulation 3-2.One imitates inspissator fluid storage compartment 1-1 communicates through pipeline with two effect inspissator fluid storage compartment 2-1 and triple effect inspissator fluid storage compartment 3-1; Protein liquid at first gets into the fluid storage compartment 3-1 of triple effect inspissator; The fluid storage compartment 2-1 that gets into two effect inspissators then just gets into the fluid storage compartment 1-1 of an effect inspissator at last, and direction and thermal current that protein liquid gets into inspissator pass through the in the opposite direction of inspissator.The structure of two effect inspissators 2 is identical with an effect inspissator 1; Imitate a part of condensation of the vapours after the exchange among the inspissator 1-3 of switch room and be that condensed water is discharged from condensate pipe 1-9 one; A part of vapours is through the heat-exchanging chamber 2-3 of blast pipe 1-5 row to two effect inspissators; Here imitate the protein liquid that circulates among the inspissator tubulation 2-2 and carry out heat exchange with two; Evaporation also concentrates gradually, imitates a part of condensation of the vapours after the exchange among the inspissator 2-3 of switch room and is that condensed water is discharged from condensate pipe 2-8 two.Vapours after remaining the utilization enters two through blast pipe 2-4 and imitates condensers 4, obtains condensation here and becomes water and cleaned air is discharged.Heated protein liquid produces hot-air too in two effect inspissators 2; These hot-airs are arranged to vapour liquid separator 2-6 through the elementary blast pipe 2-5 of two effect inspissators; Here vapour-liquid obtains separating; Liquid flows back to fluid storage compartment 2-1, and gas carries out heat exchange through the heat-exchanging chamber 3-3 that secondary blast pipe 2-7 gets into the triple effect inspissator with the protein liquid that circulates among the triple effect inspissator tubulation 3-2; Evaporation also concentrates gradually, and the vapours after triple effect inspissator effect is changed chamber 3-3 exchange is condensed into water and from condensate pipe 3-7, discharges.The vapours that is produced behind the heated protein liquid is arranged to vapour liquid separator 3-5 through elementary blast pipe 3-4; Here vapour-liquid obtains separating; Liquid flows back to fluid storage compartment 3-1, and gas enters in the triple effect condenser 5, here through secondary blast pipe 3-6; Become water through the condensation some and discharge, a part of gas is taken out after the washing of pond through vavuum pump 6 and is discharged.Vavuum pump 6 makes the inside of triple effect condenser 5 and triple effect inspissator 3 form subnormal ambient at work, also makes the fluid storage compartment 1-1 of an effect inspissator, and the fluid storage compartment 2-1 of two effect inspissators has formed subnormal ambient.The work of blower fan 7 simultaneously also makes two to imitate the heat-exchanging chamber 2-3 of inspissator and the heat-exchanging chamber 1-3 formation subnormal ambient of an effect inspissator.Be more conducive to flowing of vapours and hot-air like this, also be more conducive to flowing of protein liquid.
The utility model is work like this: at first start vavuum pump 6 and blower fan 7, make the inside of triple effect condenser 5 and triple effect inspissator 3 form subnormal ambient, also make the fluid storage compartment 1-1 of an effect inspissator, the fluid storage compartment 2-1 of two effect inspissators has formed subnormal ambient.Also make two to imitate the heat-exchanging chamber 2-3 of inspissator and the heat-exchanging chamber 1-3 formation subnormal ambient of an effect inspissator.Opening input duct makes protein liquid get into triple effect inspissator fluid storage compartment 3-1; Two imitate concentrate fluid storage compartment 2-1 and imitates inspissator fluid storage compartment 1-1; And the ON cycle pump circulates protein liquid in the tubulation of three inspissators; Open air inlet pipe 1-4, make the waste hot steam that is produced behind the heat drying fish meal get into one and imitate the inspissator 1-3 of switch room, carry out heat exchange with the protein liquid that in an effect inspissator tubulation 1-2, circulates; Make the protein liquid evaporation and concentration, the condensed water that produces after the heat exchange is discharged from condensate pipe 1-9.A part of vapours second use is through the heat-exchanging chamber 2-3 of blast pipe 1-5 row to two effect inspissators; Here imitate the protein liquid that circulates among the inspissator tubulation 2-2 and carry out heat exchange with two; Make the protein liquid evaporation and concentration, the condensed water that produces after the heat exchange is discharged from condensate pipe 2-8, and the vapours after remaining the utilization enters two through blast pipe 2-4 and imitates condenser 4; Obtain condensation here and become water and cleaned air discharge; Because vapours is fully utilized, the fish meal fishy odor that is contained in the steam is complete by basic absorption, and the gas of discharge no longer includes the off-odor of fish meal.Imitate inspissator 1 and two one and imitate the protein liquid that inspissator 2 is heated evaporation; Has higher temperature equally; The steam that these high temperature produced enters among the vapour liquid separator 1-7 through the elementary blast pipe 1-6 of an effect inspissator, and vapour-liquid obtains separating in vapour liquid separator 1-7, and liquid passes back into fluid storage compartment 1-1; Hot-air enters the heat-exchanging chamber 3-3 of triple effect inspissator through secondary blast pipe 1-8; Carry out heat exchange with the protein liquid among three grades of inspissator tubulation 3-2, also the elementary blast pipe 2-5 through two effect inspissators arranges to vapour liquid separator 2-6, and here vapour-liquid obtains separating; Liquid flows back to fluid storage compartment 2-1; Gas carries out heat exchange through the heat-exchanging chamber 3-3 of secondary blast pipe 2-7 entering triple effect inspissator with the protein liquid that circulates among the triple effect inspissator tubulation 3-2, and acting in conjunction makes the protein liquid among the triple effect inspissator fluid storage compartment 3-1 obtain evaporation and concentration.Vapours after the utilization is condensed into condensed water and discharges from condensate pipe 3-7; To vapour liquid separator 3-5, here vapour-liquid obtains separating a part of gas through elementary blast pipe 3-4 row, and liquid flows back to fluid storage compartment 3-1; Gas enters in the triple effect condenser 5 through secondary blast pipe 3-6; Here, become water through the condensation some and discharge, a part of gas is taken out after the washing of pond through vavuum pump 6 and is discharged.
After the evaporation and concentration through the multiple-effect inspissator, protein liquid is brought up to 28-30% from initial solid content 4-5%, concentrates then and can become the fish meal finished product through drying in the entering dryer of fish meal again through vacuum again.
Claims (1)
1. fish meal protein liquid concentrating recovery device; It is characterized in that imitating inspissator (1) by one is connected through blast pipe (1-5) and two effect inspissators (2); One imitates inspissator (1) is communicated with triple effect inspissator (3) through elementary blast pipe (1-6), vapour liquid separator (1-7) and secondary blast pipe (1-8); Two imitate inspissator (2) also is connected with triple effect inspissator (3) through elementary blast pipe (2-5), vapour liquid separator (2-6) and secondary blast pipe (2-7); One effect inspissator (1), two is imitated fluid storage compartment (1-1), (2-1) of inspissators (2) and triple effect inspissator (3) and (3-1) is connected through water pipe; Triple effect inspissator (3) is connected with triple effect condenser (5) through elementary blast pipe (3-4), vapour liquid separator (3-5) and secondary blast pipe (3-6); Vavuum pump (6) is connected with triple effect condenser (5) through tracheae; Make triple effect condenser (5), triple effect inspissator (3); And one imitate inspissator fluid storage compartment (1-1) and two and imitate inspissator fluid storage compartments (2-1) and can both form subnormal ambient, and two imitate inspissators (2) imitates condensers (4) through blast pipe (2-4) and two and is connected, and blower fan (7) makes the heat-exchanging chamber (2-3) of two effect inspissators and heat-exchanging chamber (1-3) the formation subnormal ambient of an effect inspissator through the tracheae of two effect condensers (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203729848U CN202286145U (en) | 2011-10-06 | 2011-10-06 | Device for recycling liquid protein in fish meal through concentration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203729848U CN202286145U (en) | 2011-10-06 | 2011-10-06 | Device for recycling liquid protein in fish meal through concentration |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202286145U true CN202286145U (en) | 2012-07-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203729848U Expired - Lifetime CN202286145U (en) | 2011-10-06 | 2011-10-06 | Device for recycling liquid protein in fish meal through concentration |
Country Status (1)
| Country | Link |
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| CN (1) | CN202286145U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103691137A (en) * | 2013-12-26 | 2014-04-02 | 龙源海洋生物股份有限公司 | Fish pressed liquor concentrator |
| CN104147803A (en) * | 2014-08-07 | 2014-11-19 | 四川兴晟锂业有限责任公司 | Tri-effect concentration and crystallization equipment and method of lithium hydroxide |
| CN107384785A (en) * | 2017-06-02 | 2017-11-24 | 肥城金塔机械科技有限公司 | For the extracting method of marine animal albumen, device and its application |
| CN108147607A (en) * | 2018-01-31 | 2018-06-12 | 江苏深蓝远洋渔业有限公司 | A kind of boat-carrying euphausia superba powder process equipment waste water treatment system |
| CN109045932A (en) * | 2018-09-20 | 2018-12-21 | 岭商（浙江）生物科技有限公司 | A kind of exhaust treatment system and its treatment process of fish meal |
-
2011
- 2011-10-06 CN CN2011203729848U patent/CN202286145U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103691137A (en) * | 2013-12-26 | 2014-04-02 | 龙源海洋生物股份有限公司 | Fish pressed liquor concentrator |
| CN104147803A (en) * | 2014-08-07 | 2014-11-19 | 四川兴晟锂业有限责任公司 | Tri-effect concentration and crystallization equipment and method of lithium hydroxide |
| CN107384785A (en) * | 2017-06-02 | 2017-11-24 | 肥城金塔机械科技有限公司 | For the extracting method of marine animal albumen, device and its application |
| CN108147607A (en) * | 2018-01-31 | 2018-06-12 | 江苏深蓝远洋渔业有限公司 | A kind of boat-carrying euphausia superba powder process equipment waste water treatment system |
| CN109045932A (en) * | 2018-09-20 | 2018-12-21 | 岭商（浙江）生物科技有限公司 | A kind of exhaust treatment system and its treatment process of fish meal |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Beihai Acer fish meal equipment Co., Ltd. Assignor: He Xinguo Contract record no.: 2013450000055 Denomination of utility model: Device for recycling liquid protein in fish meal through concentration Granted publication date: 20120704 License type: Exclusive License Record date: 20130609 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120704 |