CN2910940Y - Production line for extraction of shrimp head peptide protein and chitin - Google Patents
Production line for extraction of shrimp head peptide protein and chitin Download PDFInfo
- Publication number
- CN2910940Y CN2910940Y CN 200620061500 CN200620061500U CN2910940Y CN 2910940 Y CN2910940 Y CN 2910940Y CN 200620061500 CN200620061500 CN 200620061500 CN 200620061500 U CN200620061500 U CN 200620061500U CN 2910940 Y CN2910940 Y CN 2910940Y
- Authority
- CN
- China
- Prior art keywords
- chitin
- production line
- peptide protein
- shrimp head
- shrimp
- 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
Images
Abstract
The utility model discloses a production line of enzymatic method fractionating shrimp head little peptide protein and chitin prime, comprising a enzymatic hydrolysis reactionary pot respectively connected with a filter, a medium storage cylinder and a dual effect evaporator by a transportation device to form a branch production line of the little peptide protein and respectively connected with a separator, a rinsing machine, a centrifuging machine, a dryer and a packaging machine to form a branch production line of the chitin prime. The utility model realizes the mechanized continuous operation with a high production efficiency and zero pollution which can reduces the labor intensity of the workers significantly and improves the working efficiency greatly and not only eliminates the harm of the processing remains of the shrimp to the environment but also creates the condition of the exploitation and utilization of the chitosan and other new materials, which is favourable to the environmental protection.
Description
Technical field
The utility model relates to the production line that branch is carried shrimp head peptide protein and chitin.
Background technology
The residuum of prawn processing, as bright shrimp head capsule, skin etc., easy smelly living maggot, it is big to focus on difficulty, always is aquatic products processing factory stubborn problem.General producer is dried the back and sells as feedstuff raw material, and economic benefit is extremely low.Also have indivedual factories to attempt removing protein and calcareous, do the chitin export trade after cleaning is dried, but this treatment process one has produced a large amount of acidic and alkaline waste water dischargings, and environment is polluted with the method for acid, alkali; Two protein that wherein are rich in are wasted in vain and stench take place, and exist the utilization of resources to be worth low problem equally.
Summary of the invention
The purpose of this utility model is to provide a kind of work efficiency that significantly improves, and helps environment protection, and the branch that economic worth is high is carried the production line of shrimp head peptide protein and chitin.
In order to reach the foregoing invention purpose, the utility model has adopted following technical scheme: the enzyme process branch is carried the production line of shrimp head peptide protein and chitin, it is characterized in that: comprise an enzyme digestion reaction jar, constitute into little peptide protein with the strainer that links to each other successively by handling equipment, middle storage tank, double-effect evaporator and wrapping machine and produce separated time; And constitute chitin with the separating machine that links to each other successively by handling equipment, fulling mill, whizzer, moisture eliminator and wrapping machine and produce separated time.
The utility model is used modern biotechnology at the present situation of like product technology, designs the enzyme process branch voluntarily and carries shrimp head peptide protein cream and chitin production line, realized the mechanize operate continuously, have the production efficiency height, pollution-free, alleviated the advantage of working strength of workers widely.Culture in coastal area of china area on the south the utility model, and the prawn industrial wood waste---shrimp head capsule (skin) is a raw material, adopt the zymochemistry biotechnology to divide the specific equipment of carrying, can significantly improve work efficiency, not only eliminated the harm of prawn industrial wood waste contaminate environment, also precondition has been created in the development and use of novel materials such as chitosan, help environment protection, isolated little peptide protein condensed cream delicate flavour is dense, purity is high, can be used as the phagostimulant of animal-feed; Removed albumen and calcareous dried small shrimp (chitin) deep processing is a chitosan, purposes is very extensive, and economic worth is high.A kind of raw material is made two products, and economic benefit is fairly obvious.Prove through production test, adopt this production line branch to carry shrimp head peptide protein cream and chitin, every service data meets the index that when design set, and is better than state of the art of the same trade, the shrimp head peptide protein cream that produces and chitin product all meet national correlation technique standard.
Description of drawings
Fig. 1 is the utility model production line synoptic diagram.
Embodiment
Be illustrated in figure 1 as complete shrimp head peptide protein cream and chitin production line, comprise an enzyme digestion reaction jar 1, and successively sieve plate strainer 2, middle storage tank 3, double-effect evaporator 4 and portioning machine 5 are linked to be little peptide protein production separated time by handling equipment; And by horizontal centrifuge 6, fulling mill 7, whizzer 8, moisture eliminator structure 9 and wrapping machine 10 formation chitins production separated times.
The residuum of prawn processing---bright shrimp head capsule (skin) raw material quantitatively is transported in the jacketed type stainless steel enzyme digestion reaction jar 1 of volume V=3 cubic metre with lift, add proper amount of clear water, proteolytic enzyme again, through operant responses such as stirring, temperature adjustment, insulation enzymolysis, filter to isolate the little peptide protein solution 11 of enzymolysis.Device has blade agitator, bottom to be provided with the blowing quick opening valve in the retort 1, also with steam, cold and hot water heating temperature adjustment function.
The enzymolysis protein solution 11 (acidified aqueous solution) of discharging from retort bottom is behind flat screen panel filter 2 elimination impurity 22, and it is that 10 cubic metres process tank 3 is temporary that the refined liquid 21 that obtains flows into volume automatically by high potential difference.
With the mode of centrifugal water pump or vacuum intake, the refined liquid 21 that process tank is temporary is transported in the double-effect evaporator 4, carries out vacuum concentration, removes large quantity of moisture to dry matter content and be 50% little peptide protein cream 41, and waste water 42 is drained.Little peptide protein cream 41 through being up to the standards is made little peptide protein cream finished product 51 through portioning machine 5.Double-effect evaporator 4 is made for stainless steel, and heating-surface area is 40 square metres, and heating steam pressure is 1 kilogram/square centimeter, and maximum vacuum is 650 a millimeters/mercury column.
With adding the proper quantity of lye neutralization through the dried small shrimp after enzymolysis, the acidifying 12 in the enzyme digestion reaction jar 1, flow into the sieve plate strainer together with neutralizer, to put into again and remove its surperficial raffinate in the horizontal centrifuge 6, raffinate 62 is discharged.Whizzer rotor diameter is 600 millimeters, 800 rev/mins of rotating speeds.
The dried small shrimp 61 that has removed raffinate is changed over to usefulness clear water flush away impurity in the rotary type fulling mill 7, and waste water 72 is discharged.The fulling mill volume is 10 cubic metres, and supporting have the stirring of horizontal blade, self-priming to change water and automatic discharge device.
Clean qualified dried small shrimp mixed solution 71 and quantitatively flow into 8 dehydrations of tripodia vertical centrifugal machine through the automatic discharge device, waste water 82 is discharged.1000 millimeters of whizzer 8 rotating cylinder diameters, 3 millimeters of mesh sizes, 3000 rev/mins of rotating speeds.
It is dry that the wet dried small shrimp 81 (being the chitin work in-process) that has removed surface-moisture is sent into hot-air drier 9 temperature that weighs, to moisture less than 10%, and, obtain chitin product 101 through portioning machine 10.Hot-air drier 9 areas are 40 square metres, heating steam pressure 1 kilograms per centimeter square, wind-warm syndrome is 50～70 ℃, air quantity be 2700 cubic metres/time.
Claims (3)
1, the enzyme process branch is carried the production line of shrimp head peptide protein and chitin, it is characterized in that:
Comprise an enzyme digestion reaction jar,
Constitute into little peptide protein with the strainer that links to each other successively by handling equipment, middle storage tank, double-effect evaporator and wrapping machine and produce separated time; And
Constitute chitin with the separating machine that links to each other successively by handling equipment, fulling mill, whizzer, moisture eliminator and wrapping machine and produce separated time.
2, enzyme process branch according to claim 1 is carried the production line of shrimp head peptide protein and chitin, it is characterized in that: be provided with blade agitator in the described enzymolysis reactor, the bottom is provided with the blowing quick opening valve.
3, enzyme process branch according to claim 1 is carried the production line of shrimp head peptide protein and chitin, it is characterized in that: described strainer is the flat screen panel filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620061500 CN2910940Y (en) | 2006-07-11 | 2006-07-11 | Production line for extraction of shrimp head peptide protein and chitin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620061500 CN2910940Y (en) | 2006-07-11 | 2006-07-11 | Production line for extraction of shrimp head peptide protein and chitin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2910940Y true CN2910940Y (en) | 2007-06-13 |
Family
ID=38132799
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620061500 Expired - Fee Related CN2910940Y (en) | 2006-07-11 | 2006-07-11 | Production line for extraction of shrimp head peptide protein and chitin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2910940Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102850448A (en) * | 2012-08-24 | 2013-01-02 | 李晓航 | Process for extracting shrimp protein by utilizing waste liquid from immersion cleaning of shrimp meat and headless shrimp |
| CN103749938A (en) * | 2014-01-24 | 2014-04-30 | 张延� | Nut protein extracting device with secondary teeth and gas blowing stirring device |
-
2006
- 2006-07-11 CN CN 200620061500 patent/CN2910940Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102850448A (en) * | 2012-08-24 | 2013-01-02 | 李晓航 | Process for extracting shrimp protein by utilizing waste liquid from immersion cleaning of shrimp meat and headless shrimp |
| CN103749938A (en) * | 2014-01-24 | 2014-04-30 | 张延� | Nut protein extracting device with secondary teeth and gas blowing stirring device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US8663952B2 (en) | Method of producing corn starch by enzymatic process | |
| CN101407832B (en) | Method for producing chitin, calcium citrate and protein powder | |
| CN102660606B (en) | Bio-preparation method for production of high-purity xylo-oligosaccharide and coproduction of arabinose and xylose | |
| CN101787382B (en) | Method for recovering coin protein sugar dregs and preparing protein nitrogen sources and nitrogen-containing syrup | |
| CN103302080B (en) | A kind of preparation method of egg-shell meal and process equipment | |
| CN101649336B (en) | Novel process for producing sodium heparin | |
| CN103254320A (en) | Method for producing corn starch by utilizing enzymic method | |
| CN102351944B (en) | Method for extracting alfalfa leaf protein by ultrasonic-assisted enzyme process | |
| CN110256603A (en) | A kind of-two step enzyme method coupling of shrimp and crab shells hydro-thermal prepares the methods and applications of chitin and chitosan | |
| CN101560270A (en) | Chitin production method with energy-saving and emission-reduction | |
| CN102086464A (en) | Method for preparing chitin | |
| CN1814772A (en) | Animal shell substance treating method and device | |
| CN86108557A (en) | With proteinaceous waste material is material, enzyme method method of extracting protein hydrolystate and products thereof | |
| CN2910940Y (en) | Production line for extraction of shrimp head peptide protein and chitin | |
| CN105017433A (en) | Process for comprehensively utilizing wild acorns to process and extract tannin and starch | |
| CN101775085B (en) | Preparation method of fly maggot chitosan | |
| CN111171163B (en) | Potato starch production line and production method thereof | |
| CN103520979A (en) | Special vacuum-type drum filter for treating ultrafiltration tank bottom substances and treatment method of ultrafiltration tank bottom substances | |
| CN101659712A (en) | Method for extracting sodium heparin crude product by using porcine intestine | |
| CN202576308U (en) | Device for extracting shrimp protein from acid-base hydrolysate | |
| CN201952420U (en) | Sugar extracting system of grain emulsion | |
| CN209219218U (en) | A kind of digested tankage production equipment | |
| CN108912244B (en) | Method for extracting chitin from crab shells by one-step decalcification, deproteinization and fat removal | |
| CN102241789A (en) | Chitosan | |
| CN1865291A (en) | Clean preparation process of chitin |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070613 Termination date: 20120711 |