CN204417512U - Be applicable to the enzymatic hydrolysis system of rabbit plasma enzymolysis - Google Patents
Be applicable to the enzymatic hydrolysis system of rabbit plasma enzymolysis Download PDFInfo
- Publication number
- CN204417512U CN204417512U CN201420807899.3U CN201420807899U CN204417512U CN 204417512 U CN204417512 U CN 204417512U CN 201420807899 U CN201420807899 U CN 201420807899U CN 204417512 U CN204417512 U CN 204417512U
- Authority
- CN
- China
- Prior art keywords
- reactor
- enzymatic hydrolysis
- constant temperature
- hot water
- temperature water
- 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.)
- Active
Links
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Processing Of Solid Wastes (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model discloses a kind of enzymatic hydrolysis system being applicable to rabbit plasma enzymolysis, it comprises constant temperature water tank, reactor, PLC control system, supplied materials receiving tank, one end of described constant temperature water tank is provided with hot water pump, hot water pump is connected with the upper end of reactor by thermostat(t)ed water pipeline, the other end of described constant temperature water tank is connected with the lower end of reactor by attemperater road, described reactor top is provided with the step-down gear be connected with reactor, tensimeter, inside is provided with the agitating vane be connected with step-down gear, described reactor top, bottom is respectively equipped with feed pipe, discharge pipe, described supplied materials receiving tank is provided with feeding pump, described feeding pump is connected with the feed pipe of reactor, described PLC control system and hot water pump, reactor connects.This enzymatic hydrolysis system structure is simple, reasonable in design, the enzyme digestion reaction in effective controlled enzymatic hydrolysis tank.
Description
Technical field
The utility model belongs to the equipment of industrial product, is specifically related to a kind of enzymatic hydrolysis system being applicable to rabbit plasma enzymolysis.
Background technology
Enzymatic vessel as industrial equipments widely used in industry, each industry can according to self industry need enzymatic vessel is transformed, to adapt to the application of the industry.For not having special enzymatic hydrolysis system from the field of rabbit plasma being carried out to enzymolysis, existing enzymatic hydrolysis system is not suitable for this area.
Summary of the invention
In order to overcome the problems referred to above that prior art field exists, the purpose of this utility model is, provides a kind of enzymatic hydrolysis system being applicable to rabbit plasma enzymolysis, solves the enzymatic hydrolysis system of passing on Gong and is not suitable for the problem of rabbit plasma being carried out to enzymolysis field.
The enzymatic hydrolysis system of what the utility model provided be applicable to rabbit plasma enzymolysis, it comprises constant temperature water tank, reactor, PLC control system, supplied materials receiving tank, one end of described constant temperature water tank is provided with hot water pump, hot water pump is connected with the upper end of reactor by thermostat(t)ed water pipeline, the other end of described constant temperature water tank is connected with the lower end of reactor by attemperater road, described reactor top is provided with the step-down gear be connected with reactor, tensimeter, inside is provided with the agitating vane be connected with step-down gear, described reactor top, bottom is respectively equipped with feed pipe, discharge pipe, described supplied materials receiving tank is provided with feeding pump, described feeding pump is connected with the feed pipe of reactor, described PLC control system and hot water pump, reactor connects.
Described constant temperature water tank, reactor, supplied materials collection box are equipped with valve.
The enzymatic hydrolysis system of what the utility model provided be applicable to rabbit plasma enzymolysis, its beneficial effect is, this enzymatic hydrolysis system structure is simple, reasonable in design, the enzyme digestion reaction in effective controlled enzymatic hydrolysis tank.
Accompanying drawing explanation
Fig. 1 is the one-piece construction schematic diagram of the utility model embodiment.
Mark in figure:
1. constant temperature water tank; 2. reactor; 3.PLC Controlling System; 4. supplied materials receiving tank; 5. hot water pump; 6. thermostat(t)ed water pipeline; 7. step-down gear; 8. tensimeter; 9. valve; 10. agitating vane; 11. feed pipes; 12. discharge pipes; 13. feeding pumps; 14. attemperater roads.
Embodiment
With reference to the accompanying drawings, in conjunction with the embodiments, to the enzymatic hydrolysis system being applicable to rabbit plasma enzymolysis that the utility model provides, be described in detail.
Embodiment
With reference to Fig. 1, the enzymatic hydrolysis system being applicable to rabbit plasma enzymolysis of the present embodiment, it comprises constant temperature water tank 1, reactor 2, PLC control system 3, supplied materials receiving tank 4, one end of described constant temperature water tank 1 is provided with hot water pump 5, hot water pump 5 is connected with the upper end of reactor 4 by thermostat(t)ed water pipeline 6, the other end of described constant temperature water tank 1 is connected with the lower end of reactor 2 by attemperater road 14, described reactor 2 top is provided with the step-down gear 7 be connected with reactor 2, tensimeter 8, inside is provided with the agitating vane 10 be connected with step-down gear 7, described reactor 2 top, bottom is respectively equipped with feed pipe 11, discharge pipe 12, described supplied materials receiving tank 4 is provided with feeding pump 13, described feeding pump 13 is connected with the feed pipe 11 of reactor 2, described PLC control system 3 and hot water pump 5, reactor 2 connects.
Described constant temperature water tank 1, reactor 2, supplied materials collection box 4 are equipped with valve 9.
Raw material enters supplied materials receiving tank 4 through pulverizing after after homogeneous interpolation bacterial classification, and be transported to reactor 2 by feeding pump 13, feed pipe 11, reaction process needs agitating vane 10 constantly to stir; Constant temperature water tank 1 for reactor 2 provide temperature ensure hot water, hot water enters reactor 4(upper entering and lower leaving by hot water pump 5 self-heat conserving waterpipe 14, in attemperater road 14, water flow velocity ensures Inlet and outlet water almost isothermal very soon), PLC robot control system(RCS) 3 Ligature still 2 and each pipeline and valve 9, control the operation of whole system.
Claims (2)
1. one kind is applicable to the enzymatic hydrolysis system of rabbit plasma enzymolysis, it is characterized in that: it comprises constant temperature water tank, reactor, PLC control system, supplied materials receiving tank, one end of described constant temperature water tank is provided with hot water pump, hot water pump is connected with the upper end of reactor by thermostat(t)ed water pipeline, the other end of described constant temperature water tank is connected with the lower end of reactor by attemperater road, described reactor top is provided with the step-down gear be connected with reactor, tensimeter, inside is provided with the agitating vane be connected with step-down gear, described reactor top, bottom is respectively equipped with feed pipe, discharge pipe, described supplied materials receiving tank is provided with feeding pump, described feeding pump is connected with the feed pipe of reactor, described PLC control system and hot water pump, reactor connects.
2. the enzymatic hydrolysis system being applicable to rabbit plasma enzymolysis according to claim 1, is characterized in that: described constant temperature water tank, reactor, supplied materials collection box are equipped with valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420807899.3U CN204417512U (en) | 2014-12-19 | 2014-12-19 | Be applicable to the enzymatic hydrolysis system of rabbit plasma enzymolysis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420807899.3U CN204417512U (en) | 2014-12-19 | 2014-12-19 | Be applicable to the enzymatic hydrolysis system of rabbit plasma enzymolysis |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204417512U true CN204417512U (en) | 2015-06-24 |
Family
ID=53467899
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420807899.3U Active CN204417512U (en) | 2014-12-19 | 2014-12-19 | Be applicable to the enzymatic hydrolysis system of rabbit plasma enzymolysis |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204417512U (en) |
-
2014
- 2014-12-19 CN CN201420807899.3U patent/CN204417512U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102220223B (en) | Solid-state fermentation material processing device | |
| CN102776075B (en) | Interactive turbulent flow reaction device | |
| CN204417512U (en) | Be applicable to the enzymatic hydrolysis system of rabbit plasma enzymolysis | |
| CN203494457U (en) | Automatic energy-saving modified rock asphalt production equipment | |
| CN203545858U (en) | Improved type enamel anaerobic fermentation tank | |
| CN202538667U (en) | Alternative jet flow disturbance system | |
| CN103881868B (en) | Rice milk zero release recycling system | |
| CN203291262U (en) | Energy-saving fermentation culture-medium continuous sterilization system | |
| CN202594787U (en) | Device for producing granular feed-grade calcium hydrogen phosphate by utilizing wet-process phosphoric acid | |
| CN201784052U (en) | Metering conveying tank | |
| CN204934145U (en) | Based on the gas purging power set improving liquid feeding pipe cleannes | |
| CN203833936U (en) | Device for liquid two-phase anaerobic fermentation differential-pressure feeding and discharging | |
| CN104531505B (en) | To prepare burden in neomycinsulphate fermentative production water-adding system and method | |
| CN203321784U (en) | Vacuum pump cooling water recovery device | |
| CN203593710U (en) | Reaction device used for preparing L-carnitine | |
| CN203971895U (en) | Many raw materials of reactor drip system | |
| CN205133480U (en) | Device is added with alkali to modified starch production | |
| CN104474986B (en) | The continuous sulfonation production device of gaseous sulfur trioxide | |
| CN203960087U (en) | High pressure alcohol wash system | |
| CN204278292U (en) | The mixing device that a kind of processed polyesters bottle sheet flow is adjustable | |
| CN203862230U (en) | Water-saving cooling device | |
| CN203540716U (en) | Flotation gravity flow medicine adding device | |
| CN203346400U (en) | Bioreactor | |
| CN203580094U (en) | Water supply and discharge device of material strip cooling bath | |
| CN203425792U (en) | Multi-kettle feeding full-automatic continuous production device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |