CN203582868U - Continuous enzyme hydrolysis device for polypeptides - Google Patents
Continuous enzyme hydrolysis device for polypeptides Download PDFInfo
- Publication number
- CN203582868U CN203582868U CN201320741871.XU CN201320741871U CN203582868U CN 203582868 U CN203582868 U CN 203582868U CN 201320741871 U CN201320741871 U CN 201320741871U CN 203582868 U CN203582868 U CN 203582868U
- Authority
- CN
- China
- Prior art keywords
- enzyme hydrolysis
- valve
- enzymolysis
- enzymatic vessel
- continuous
- 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 - Lifetime
Links
- 238000006460 hydrolysis reaction Methods 0.000 title claims abstract description 34
- 230000007062 hydrolysis Effects 0.000 title claims abstract description 33
- 108090000765 processed proteins & peptides Proteins 0.000 title claims abstract description 17
- 229920001184 polypeptide Polymers 0.000 title claims abstract description 13
- 102000004196 processed proteins & peptides Human genes 0.000 title claims abstract description 13
- 102000004190 Enzymes Human genes 0.000 title abstract description 18
- 108090000790 Enzymes Proteins 0.000 title abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000000523 sample Substances 0.000 claims abstract description 11
- 230000002255 enzymatic effect Effects 0.000 claims description 43
- 238000004321 preservation Methods 0.000 claims description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 5
- 230000008719 thickening Effects 0.000 claims description 5
- 239000000463 material Substances 0.000 abstract description 13
- 230000017854 proteolysis Effects 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000002994 raw material Substances 0.000 abstract description 4
- 238000010924 continuous production Methods 0.000 abstract description 2
- 239000003814 drug Substances 0.000 abstract description 2
- 235000013305 food Nutrition 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 abstract 5
- 238000001514 detection method Methods 0.000 abstract 3
- 238000007599 discharging Methods 0.000 abstract 2
- 238000003889 chemical engineering Methods 0.000 abstract 1
- 229940079593 drug Drugs 0.000 abstract 1
- 238000009413 insulation Methods 0.000 abstract 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 abstract 1
- 241000196324 Embryophyta Species 0.000 description 7
- 102000035195 Peptidases Human genes 0.000 description 5
- 108091005804 Peptidases Proteins 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 241000894007 species Species 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 108010082495 Dietary Plant Proteins Proteins 0.000 description 1
- 108010064851 Plant Proteins Proteins 0.000 description 1
- 108010073771 Soybean Proteins Proteins 0.000 description 1
- 235000021120 animal protein Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001976 enzyme digestion Methods 0.000 description 1
- 235000021118 plant-derived protein Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 235000019710 soybean protein Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model discloses a continuous enzyme hydrolysis device for polypeptides. The continuous enzyme hydrolysis device comprises a enzyme hydrolysis tank, wherein the enzyme hydrolysis tank is provided with a feeding opening and a water feeding valve; the enzyme hydrolysis tank is connected with a disk centrifuging machine by a discharging valve; the disk centrifuging machine is provided with an enzyme hydrolysis liquid heavy-phase outlet communicated with an enzyme hydrolysis liquid heavy-phase storage tank, so as to be communicated with the enzyme hydrolysis tank by a material conveying pump. The feeding opening, the water feeding valve and a variable frequency motor are arranged on the top of the enzyme hydrolysis tank; a jacket heat-insulation layer is arranged on the outer part of the enzyme hydrolysis tank; a temperature detection probe is arranged on the tank wall of the enzyme hydrolysis tank; the temperature detection probe is connected with a temperature controller by a lead wire and a discharging valve is arranged at the bottom of the temperature detection probe. The disk centrifuging machine is additionally provided with an enzyme hydrolysis liquid light-phase outlet to be communicated with an enzyme hydrolysis liquid light-phase storage tank, so as to convey light-phase liquid to concentration equipment. According to the continuous enzyme hydrolysis device, the middle intermittent production problems of animal and plant proteolysis are solved and the utilization rate of raw materials and the utilization rate of equipment are greatly improved; the requirements of the continuous production of the animal and plant proteolysis are met. The continuous enzyme hydrolysis device for the polypeptides has the characteristics that production is continuous, operation is simple, use is safe, price is low and popularization is easy, and can be widely applied to industries including foods, medicines and chemical engineering.
Description
Technical field
The utility model relates to a peptide species continuous enzymolysis and hydrolysis device, is specially adapted to continuous enzymolysis and hydrolysis reaction, belongs to biochemical reactor field.
Background technology
The enzymic hydrolysis of animal and plant albumen is to take animal and plant as raw material, through the effect of enzyme, the process being hydrolyzed under certain temperature condition.Traditional is moving, the enzymolysis process of vegetable-protein adopts batch operation more, be disposable feeding intake, enzyme-added, hydrolysis, separated, enzyme etc. goes out, and exist in the isolated enzymolysis solution heavy phase part of institute, be not hydrolyzed in a large number sufficient material, if being hydrolyzed to sufficient material, this part does not turn back to enzymatic vessel, and supplementary partial material, proteolytic enzyme and water, make the material in enzymatic vessel keep certain concentration continuation enzymolysis can greatly improve the utilization ratio of raw material and the utilization ratio of equipment, therefore, adopt polypeptide continuous enzymolysis and hydrolysis device, can make enzyme digestion reaction carry out more thoroughly, reduce production costs.
Summary of the invention
The purpose of this utility model is to provide the polypeptide continuous enzymolysis and hydrolysis device that a kind of production efficiency is high, rational in infrastructure, be easy to apply.
The technical scheme that the utility model is taked is:
This polypeptide continuous enzymolysis and hydrolysis device comprises enzymatic vessel, described enzymatic vessel is established dog-house and water intaking valve, enzymatic vessel connects disk plate centrifuge by its blow-off valve, the set enzymolysis solution heavy out of disk plate centrifuge is communicated with enzymolysis solution heavy phase basin, and the outlet of enzymolysis solution heavy phase basin is communicated with enzymatic vessel by baiting valve, material-handling pump and transfer valve.
Dog-house and water intaking valve are established in described enzymatic vessel top, and the variable-frequency electric arbor at enzymatic vessel top can drive stirring rake to rotate; Enzymatic vessel outside is provided with jacket heat-preservation layer, and jacket heat-preservation layer is provided with into and out of water valve, and enzymatic vessel tank skin place is also provided with temperature probe, and temperature probe is connected with temperature controller by wire, and blow-off valve is established in enzymatic vessel bottom.
Described water intaking valve is communicated with pure water basin.
Described disk plate centrifuge is separately established enzymolysis solution light phase export and is communicated with the light phase basin of enzymolysis solution, by the latter, enzymolysis solution is gently transported to thickening equipment mutually concentrated.
The light phase basin of described enzymatic vessel, enzymolysis solution heavy phase basin and enzymolysis solution is made by stainless steel.
In the enzymolysis operating process of animal and plant albumen, animal and plant protein material and the proteolytic enzyme of powdery are put into enzymatic vessel by the dog-house of opening, and the pure water in pure water basin is put into enzymatic vessel, the steam of opening in chuck heats the material in enzymatic vessel.Stirring rake rotates under the drive of variable-frequency motor, makes enzymolysis material and water generates relative movement disperse and heat up, and can open and close relevant valve to pilot circuit by temperature probe, temperature controller and carry out temperature adjustment after temperature reaches set(ting)value.Enzymolysis carries out after certain hour, and enzymolysis solution is discharged by the blow-off valve of enzymatic vessel bottom, by disk plate centrifuge, carries out separation, and isolated enzymolysis solution heavy phase enters enzymolysis solution heavy phase basin, and is driven in enzymatic vessel by material-handling pump.Meanwhile, by supplementing partial material and proteolytic enzyme, pure water, can realize continuous enzymolysis and produce.And isolated enzymolysis solution gently enters the light phase basin of enzymolysis solution mutually, then go thickening equipment to concentrate.
This continuous enzymolysis and hydrolysis device has solved the problem that animal and plant proteolysis discontinuous is produced preferably, and the utilization ratio of raw material and the utilization ratio of equipment are greatly improved, and has met the uninterrupted needs of producing of animal and plant proteolysis.The utlity model has continuous production, simple to operate, use safety, the cheap feature that is easy to popularization, can be widely used in the industries such as food, medicine, chemical industry.
accompanying drawing explanation
Fig. 1 is the schematic diagram of the utility model one peptide species continuous enzymolysis and hydrolysis device.
Below in conjunction with accompanying drawing, embodiment of the present utility model is described in further detail.
specific implementation method
As shown in Figure 1, polypeptide continuous enzymolysis and hydrolysis device is comprised of enzymatic vessel 1, pure water basin 4, disk plate centrifuge 13, enzymolysis solution heavy phase basin 14, the light phase basin 18 of enzymolysis solution, material-handling pump 16, valve and pipeline 20 etc.
Enzymatic vessel 1 is made by stainless steel, and dog-house 2 and water intaking valve 5 are established in enzymatic vessel 1 top, and blow-off valve 9 is established in bottom.Variable-frequency motor 3 axles at enzymatic vessel 1 top can drive stirring rake 6 to rotate, enzymatic vessel 1 outside is provided with jacket heat-preservation layer 7, jacket heat-preservation layer 7 is provided with into and out of water valve 12,8, and enzymatic vessel 1 tank skin place is also provided with temperature probe 11, and temperature probe 11 is connected with temperature controller 10 by wire.
Enzymatic vessel 1 is communicated with pure water basin 4 by set water intaking valve 5, enzymatic vessel 1 connects disk plate centrifuge 13 by its blow-off valve 9, the set enzymolysis solution heavy out of disk plate centrifuge 13 is communicated with enzymolysis solution heavy phase basin 14, and 14 outlets of enzymolysis solution heavy phase basin are communicated with enzymatic vessel 1 by baiting valve 15, material-handling pump 16 and transfer valve 17.
Disk plate centrifuge 13 is separately established enzymolysis solution light phase export and is communicated with the light phase basin 18 of enzymolysis solution, by the latter, enzymolysis solution is gently transported to thickening equipment mutually concentrated.
Enzymolysis solution heavy phase basin 14, the light phase basin 18 of enzymolysis solution are made by stainless steel.
Described connection valve all can adopt magnetic valve, and magnetic valve is controlled its on-off action by the pilot circuit being attached thereto.
Between described equipment, by stainless steel pipes, connect.
The utility model is in animal and plant proteolysis process, open the batching hole 2 on enzymatic vessel 1, the animal and plant material of powdery (as: soybean protein isolate, fishbone powder etc.) and proteolytic enzyme are put into enzymatic vessel 1, and the pure water in pure water basin 4 is put into enzymatic vessel 1, its loading amount is about 70% left and right of enzymatic vessel 1 volume.The material of opening in the 12 pairs of enzymatic vessels 1 of steam valve in chuck 7 heats.Stirring rake 6 rotates under the drive of variable-frequency motor, makes enzymolysis material and water generates relative movement disperse and heat up, and can open and close relevant valve to pilot circuit by temperature probe 11, temperature controller 10 and carry out temperature adjustment after temperature reaches set(ting)value.Enzymolysis carries out after certain hour, enzymolysis solution is discharged by the blow-off valve 9 of enzymatic vessel bottom, by disk plate centrifuge 13, carry out separation, isolated enzymolysis solution heavy phase enters enzymolysis solution heavy phase basin 14, and be driven in enzymatic vessel 1 by material-handling pump 16, meanwhile, by batching hole 2, supplement partial material and proteolytic enzyme, pure water, can realize continuous enzymolysis and produce.And isolated enzymolysis solution gently enters the light phase basin 18 of enzymolysis solution mutually, then by blow-off valve 19, go thickening equipment to concentrate.
Claims (7)
1. a peptide species continuous enzymolysis and hydrolysis device, it is characterized in that: this device comprises enzymatic vessel (1), enzymatic vessel (1) is established dog-house (2) and water intaking valve (5), enzymatic vessel (1) connects disk plate centrifuge (13) by its blow-off valve (9), the set enzymolysis solution heavy out of disk plate centrifuge (13) is communicated with enzymolysis solution heavy phase basin (14), and enzymolysis solution heavy phase basin (14) outlet is communicated with enzymatic vessel (1) by baiting valve (15), material-handling pump (16) and transfer valve (17).
2. polypeptide continuous enzymolysis and hydrolysis device according to claim 1, it is characterized in that: dog-house (2) and water intaking valve (5) are established in enzymatic vessel (1) top, variable-frequency motor (3) axle at enzymatic vessel (1) top can drive stirring rake (6) to rotate, enzymatic vessel (1) outside is provided with jacket heat-preservation layer (7), jacket heat-preservation layer (7) is provided with into and out of water valve (12,8), enzymatic vessel (1) tank skin place is also provided with temperature probe (11), temperature probe (11) is connected with temperature controller (10) by wire, and blow-off valve (9) is established in enzymatic vessel (1) bottom.
3. polypeptide continuous enzymolysis and hydrolysis device according to claim 2, is characterized in that: water intaking valve (5) is communicated with pure water basin (4).
4. polypeptide continuous enzymolysis and hydrolysis device according to claim 3, is characterized in that: disk plate centrifuge (13) is separately established enzymolysis solution light phase export and is communicated with the light phase basin of enzymolysis solution (18), by the latter, enzymolysis solution is gently transported to thickening equipment mutually concentrated.
5. polypeptide continuous enzymolysis and hydrolysis device according to claim 4, is characterized in that: enzymatic vessel (1), enzymolysis solution heavy phase basin (14), the light phase basin of enzymolysis solution (18) are made by stainless steel.
6. according to any polypeptide continuous enzymolysis and hydrolysis device described in claim 1 to 5, it is characterized in that: described connection valve all adopts magnetic valve, and magnetic valve is controlled its on-off action by the pilot circuit being attached thereto.
7. polypeptide continuous enzymolysis and hydrolysis device according to claim 6, is characterized in that: between the equipment of described connection valve and its connection, by stainless steel pipes, be connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320741871.XU CN203582868U (en) | 2013-11-22 | 2013-11-22 | Continuous enzyme hydrolysis device for polypeptides |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320741871.XU CN203582868U (en) | 2013-11-22 | 2013-11-22 | Continuous enzyme hydrolysis device for polypeptides |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203582868U true CN203582868U (en) | 2014-05-07 |
Family
ID=50580815
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320741871.XU Expired - Lifetime CN203582868U (en) | 2013-11-22 | 2013-11-22 | Continuous enzyme hydrolysis device for polypeptides |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203582868U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107674835A (en) * | 2017-09-11 | 2018-02-09 | 广西肽王生物科技有限公司 | Moringa protease method hydrolysis device |
| CN108048297A (en) * | 2017-11-20 | 2018-05-18 | 中国科学院广州能源研究所 | A kind of device applied to oxygenation pretreatment lignocellulosic enzymolysis saccharification water-saving and emission-reducing technique |
| CN108485959A (en) * | 2018-04-18 | 2018-09-04 | 浙江天联机械有限公司 | A kind of novel enzymatic hydrolysis system |
| WO2020227852A1 (en) * | 2019-05-10 | 2020-11-19 | 邦泰生物工程(深圳)有限公司 | System for large-scale production of rh2 by means of enzymatic method |
-
2013
- 2013-11-22 CN CN201320741871.XU patent/CN203582868U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107674835A (en) * | 2017-09-11 | 2018-02-09 | 广西肽王生物科技有限公司 | Moringa protease method hydrolysis device |
| CN108048297A (en) * | 2017-11-20 | 2018-05-18 | 中国科学院广州能源研究所 | A kind of device applied to oxygenation pretreatment lignocellulosic enzymolysis saccharification water-saving and emission-reducing technique |
| CN108485959A (en) * | 2018-04-18 | 2018-09-04 | 浙江天联机械有限公司 | A kind of novel enzymatic hydrolysis system |
| WO2020227852A1 (en) * | 2019-05-10 | 2020-11-19 | 邦泰生物工程(深圳)有限公司 | System for large-scale production of rh2 by means of enzymatic method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140507 |