CN208071710U - Insulation construction in three enzymes, one ferment treatment solution production system - Google Patents
Insulation construction in three enzymes, one ferment treatment solution production system Download PDFInfo
- Publication number
- CN208071710U CN208071710U CN201820282020.6U CN201820282020U CN208071710U CN 208071710 U CN208071710 U CN 208071710U CN 201820282020 U CN201820282020 U CN 201820282020U CN 208071710 U CN208071710 U CN 208071710U
- Authority
- CN
- China
- Prior art keywords
- water
- tank
- enzymatic vessel
- order
- production system
- 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
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model discloses the insulation constructions in a kind of three enzymes, one ferment treatment solution production system, the production system includes first order enzymolysis device, first order enzymolysis device includes first order enzymatic vessel, the first rabbling mechanism in first order enzymatic vessel, raw material premix tank and the second rabbling mechanism in raw material premix tank, raw material premix tank is equipped with the discharge port that mixed raw material is imported to first order enzymatic vessel, first order enzymatic vessel includes inner cavity and shell, it is closed cavity structure between inner cavity and shell, insulation construction includes constant temperature circulating water tank, first water-delivery pump, first water inlet pipe and outlet pipe, hot water in constant temperature circulating water tank is pumped by the first water inlet pipe from the bottom end of cavity structure by the first water-delivery pump, and it is recycled back in inflow thermostatical circulating water case by connecting the outlet pipe on cavity structure top.Using rational structure design, enzyme digestion reaction can be made to be constantly in the state of highly effective reaction.
Description
Technical field
The utility model belongs to production equipment heat preservation technology field, and in particular to a kind of one ferment treatment solution production system of three enzyme
In insulation construction.
Background technology
It needs to use treatment solution liquid during certain pain therapies, for the demand in market, the extensive life for the treatment of solution
It produces extremely urgent.
In the production process of three enzymes, one ferment treatment solution, need to carry out isothermal holding to enzyme digestion reaction tank, it can one
It is directly in suitable temperature range, convenient for the efficient progress of reaction.
Invention content
The utility model aims to solve at least one of the technical problems existing in the prior art.For this purpose, the utility model carries
For the insulation construction in a kind of three enzymes, one ferment treatment solution production system, it is therefore an objective to be convenient for the heat preservation of first order enzymolysis device, make enzyme
Solution reaction is efficient to be carried out.
To achieve the goals above, the technical solution that the utility model is taken is:
A kind of insulation construction in three enzymes, one ferment treatment solution production system, the production system include first order enzymolysis dress
It sets, the first order enzymolysis device includes that first order enzymatic vessel, the first rabbling mechanism, raw material in first order enzymatic vessel are pre-
Mixed tank and the second rabbling mechanism in raw material premix tank, raw material premix tank is equipped with imports first order enzymatic vessel by mixed raw material
Discharge port, the first order enzymatic vessel includes inner cavity and shell, is closed cavity structure, the guarantor between inner cavity and shell
Warm structure includes constant temperature circulating water tank, the first water-delivery pump, the first water inlet pipe and outlet pipe, and the first water-delivery pump is by constant temperature circulating water tank
Interior hot water is pumped by the first water inlet pipe from the bottom end of cavity structure, and the outlet pipe by connecting cavity structure top recycles
It passes back into constant temperature circulating water tank.
Liquid level sensor is equipped in the constant temperature circulating water tank, and constant temperature circulating water tank passes through the second water inlet pipe and outer water receiving
Source connects, and the second water inlet pipe is equipped with one-way water inlet valve.
Temperature sensor is equipped in the constant temperature circulating water tank, temperature sensor is electrically connected with the first water-delivery pump.
First rabbling mechanism includes the first stirring motor, the first agitating shaft and the first stirring blade, the first stirring electricity
Machine is connect by the first agitating shaft with the first stirring blade, and second rabbling mechanism includes the second stirring motor, the second stirring
Axis and the second stirring blade, the second stirring motor are connect by the second agitating shaft with the second stirring blade.
The first order enzymatic vessel is equipped with hydrochloric acid storage tank, is equipped in hydrochloric acid storage tank and adjusts pH in first order enzymatic vessel
The dilute hydrochloric acid of value.
The bottom inner portion of the first order enzymatic vessel is equipped with filter chamber, and level-one enzymolysis liquid ultrafiltration is equipped in the filter chamber
Film.
The filter chamber is inverted trapezoidal filter chamber.
Microorganism enzymolysis device includes ptyalin fermentation tank, pepsin fermentation tank and trypsase fermentation tank
Body is connected to raw material premix tank, by ptyalin delivery pipe, pepsin delivery pipe and trypsase delivery pipe respectively
The enzymolysis chamber and second level enzymolysis device of level-one enzymatic vessel, discharge port and the first order enzymolysis device of the raw material premix tank connect
It connects.
The beneficial effects of the utility model:Insulation construction in three enzymes, the one ferment treatment solution production system of the utility model,
It is kept the temperature by water-bath using rational structure design convenient for being operated to first order enzymatic vessel is carried out water-bath heat preservation, it can be more preferable
Controlling reaction temperature, enzyme digestion reaction can be made to be constantly in the state of highly effective reaction.
Description of the drawings
This specification includes the following drawings, and shown content is respectively:
Fig. 1 is the structural schematic diagram of the utility model.
In figure label for:
1, microorganism enzymolysis device, 2, first order enzymolysis device, 3, second level enzymolysis device, 4, principle premixing tank, 5, empty
Cavity configuration, 6, constant temperature circulating water tank, the 7, first water-delivery pump, the 8, first water inlet pipe, 9, outlet pipe, 10, liquid level sensor, 11,
Two water inlet pipes, 12, inlet valve, the 13, first stirring motor, the 14, first agitating shaft, the 15, first stirring blade, the 16, second stirring
Motor, the 17, second agitating shaft, the 18, second stirring blade, 19, vertical discharging section, 20, arcuation discharging section, 21, hydrochloric acid storage tank.
Specific implementation mode
Below against attached drawing, by the description of the embodiment, making to specific embodiment of the present utility model further detailed
Thin explanation, it is therefore an objective to help those skilled in the art to the design of the utility model, technical solution have it is more complete, accurate and
Deep understanding, and contribute to its implementation.
As shown in Figure 1, the insulation construction in a kind of three enzymes, one ferment treatment solution production system, which includes microorganism
Enzymolysis device 1 connect first order enzymolysis device 2 and second level enzymolysis device 3, first order enzymolysis dress with microorganism enzymolysis device 1
Set 2 include first order enzymatic vessel, the first rabbling mechanism in first order enzymatic vessel, raw material premix tank 4 and set on raw material it is pre-
The second rabbling mechanism in mixed tank 4, raw material premix tank 4 are equipped with the discharge port that mixed raw material is imported to first order enzymatic vessel, and second
Product after grade enzymolysis device enzymolysis, which is imported by secondary enzymolysis conveying pipeline in subsequent fermentation and separating-purifying device, is given birth to
The rich microorganism liquid of production, the production system preferably further include that the controller of work is run for controlling production system, pass through terminal control
Device processed controls each device and works start and stop opportunity, and linking discharge feeds opportunity, to realize Intelligent control.Microorganism enzymolysis device
1 is equipped with ptyalin fermentation tank, pepsin fermentation tank and trypsase fermentation tank, passes through ptyalin respectively
Delivery pipe, pepsin delivery pipe and trypsase delivery pipe are connected to raw material premix tank, first order enzymolysis device 2 and the second level
Enzymolysis device 3.
First order enzymatic vessel includes inner cavity and shell, is closed cavity structure 5, above-mentioned heat preservation knot between inner cavity and shell
Structure includes constant temperature circulating water tank 6, the first water-delivery pump 7, the first water inlet pipe 8 and outlet pipe 9, and the first water-delivery pump 7 is by thermostatical circulating water
Hot water in case 6 is pumped by the first water inlet pipe 8 from the bottom end of cavity structure, and the outlet pipe by connecting cavity structure top
9 are recycled back in inflow thermostatical circulating water case 6.
In order to avoid there is progress that is very few and influencing entire heat-insulation system, constant temperature circulating water tank 6 in the water in constant temperature water tank
It is interior to be equipped with liquid level sensor 10, and constant temperature circulating water tank is connect by the second water inlet pipe 11 with external water source, the second water inlet pipe 11
It is equipped with inlet valve 12.Inlet valve preferably uses check valve.
Preferably, temperature sensor is equipped in constant temperature circulating water tank 6, temperature sensor is electrically connected with the first water-delivery pump.It is logical
Excess temperature sensor acquires the water temperature in constant temperature circulating water tank, if temperature is less than reaction temperature, passes through constant temperature circulating water tank pair
Internal water is heated, and when reaching the required enzyme digestion reaction temperature of second level enzymatic vessel, is controlled by controller
First water-delivery pump imports the hot water in cyclic water tank in the cavity structure of second level enzymatic vessel, realizes water-bath isothermal holding.
First rabbling mechanism includes the first stirring motor 13, the first agitating shaft 14 and the first stirring blade 15, the first stirring
Motor 13 is connect by the first agitating shaft 14 with the first stirring blade 15, and the second rabbling mechanism includes the second stirring motor 16, the
Two agitating shafts 17 and the second stirring blade 18, the second stirring motor are connect by the second agitating shaft with the second stirring blade.Stirring
Axis drives rotation work, stirring motor to control motor start and stop by controller by stirring motor.The discharge port packet of first order enzymatic vessel 4
Sequentially connected vertical discharging section 19 and arcuation discharging section 20 are included, arcuation discharging section is connected by vertical discharging section and the first enzymatic vessel
It connects.By the setting of arcuation discharging section, certain cushioning effect is played to derived material body, material body is avoided to present under freely falling body
Drop causes larger shock.
The bottom inner portion of first order enzymatic vessel is equipped with filter chamber, and level-one enzymolysis liquid ultrafiltration membrane is equipped in filter chamber.The filtering
Chamber carries out installation preferably with dismountable mounting means with first order enzymatic vessel and connect, for example, clamp or by dismountable
Fastener carries out installation connection, is conveniently replaceable filter chamber.Inverted trapezoidal filter chamber is arranged in bottom end in first order enzymatic vessel, is falling
Level-one enzymolysis liquid ultrafiltration membrane to lower recess is set in trapezoidal filter chamber, convenient for increasing contact area, improves filter effect.
It is additionally provided with hydrochloric acid storage tank 21 on first order enzymatic vessel, is equipped in hydrochloric acid storage tank and adjusts pH in first order enzymatic vessel
The dilute hydrochloric acid of value.First order enzymolysis device 2 is additionally provided with to control the first temperature control device of its tank body interior reaction temperature.Temperature control fills
It sets including heating device, thermometer and the first temperature sensor for being connected to controller.It is heated up by heating devices heat, temperature
Sensor controls its temperature value in setting by the temperature feedback in first order enzymatic vessel to controller, by controller, to protect
Demonstrate,prove best reaction environment.The course of work of first order enzymolysis device is, water and certain dense is injected in the first order enzymatic vessel
The dilute hydrochloric acid of degree, adjustment reaction liquid environment pH value are 1.0 to 5.0, to ensure to activate pepsin, provide the ring suitable for decomposition
Border.A certain amount of pepsin is added, starts rabbling mechanism and stirs evenly paddle, start-up temperature controller is heated to 28 DEG C~40 DEG C guarantors
Temperature enzymolysis 2~6 hours, carries out enzyme digestion reaction, and stirring is synchronous in the process carries out, to obtain sufficient hydrolysis result.
Second level enzymolysis device includes second level enzymatic vessel, the enzyme digestion reaction pipeline in the enzymatic vessel of the second level, enzymolysis
Reacting pipe is equipped with level-one zymolyte feed inlet and the trypsase conveying mouth that is connected to trypsase delivery pipe.Trypsase is sent out
Microbial fermentation is provided in fermentation tank and generates trypsase yeasting, and by injecting sodium hydroxide water into second level enzymatic vessel
Solution adjusts pH value to 8.0 to 10, to ensure tryptic activity, provides the environment suitable for decomposition.Enzyme digestion reaction pipeline be in
The snakelike crooked pipeline being arranged in the enzymatic vessel of the second level can extend the reaction time of reactant and catalytic materials trypsase, increase
Its big exposure level, improves reaction efficiency.The waste gate of waste material after enzyme digestion reaction lower end of duct is equipped with discharge reaction.The
Secondary enzymolysis tank lower end is equipped with secondary enzymolysis object discharge port.
Above-mentioned production system is additionally provided with first order enzymolysis device 2 and second level enzymolysis dress in detection control reaction process respectively
The PH detectors for setting interior pH value, by the way that real-time detection signal is transferred to controller, when its pH value deviates the normal value of setting
When range, controller control into the first order enzymatic vessel second level enzymatic vessel supplement add corresponding dilute hydrochloric acid solution or
Sodium hydroxide solution ensures normal effective enzyme digestion reaction, improves reaction efficiency to adjust pH value to setting value.
The utility model is exemplarily described above in association with attached drawing.Obviously, the utility model implements not
It is limited by aforesaid way.As long as using the various unsubstantialities of the methodology and technical solution progress of the utility model
Improvement;Or it is not improved, above-mentioned design and technical solution by the utility model directly apply to other occasions, at this
Within the protection domain of utility model.
Claims (5)
1. the insulation construction in a kind of three enzymes, one ferment treatment solution production system, the production system includes first order enzymolysis device,
It is characterized in that:The first order enzymolysis device includes first order enzymatic vessel, the first blender in first order enzymatic vessel
Structure, raw material premix tank and the second rabbling mechanism in raw material premix tank, raw material premix tank is equipped with imports the by mixed raw material
The discharge port of level-one enzymatic vessel, the first order enzymatic vessel includes inner cavity and shell, is closed cavity between inner cavity and shell
Structure, the insulation construction include constant temperature circulating water tank, the first water-delivery pump, the first water inlet pipe and outlet pipe, and the first water-delivery pump will
Hot water in constant temperature circulating water tank is pumped by the first water inlet pipe from the bottom end of cavity structure, and by connecting cavity structure top
Outlet pipe be recycled back to flow into thermostatical circulating water case in.
2. the insulation construction in three enzymes, one ferment treatment solution production system according to claim 1, it is characterised in that:The constant temperature
Liquid level sensor is equipped in cyclic water tank, and constant temperature circulating water tank is connect by the second water inlet pipe with external water source, the second water inlet
Pipe is equipped with one-way water inlet valve.
3. the insulation construction in three enzymes, one ferment treatment solution production system according to claim 2, it is characterised in that:The constant temperature
Temperature sensor is equipped in cyclic water tank, temperature sensor is electrically connected with the first water-delivery pump.
4. the insulation construction in three enzymes, one ferment treatment solution production system according to claim 1, it is characterised in that:Described first
Rabbling mechanism includes the first stirring motor, the first agitating shaft and the first stirring blade, and the first stirring motor passes through the first agitating shaft
It being connect with the first stirring blade, second rabbling mechanism includes the second stirring motor, the second agitating shaft and the second stirring blade,
Second stirring motor is connect by the second agitating shaft with the second stirring blade.
5. the insulation construction in three enzymes, one ferment treatment solution production system according to claim 1, it is characterised in that:Described first
Grade enzymatic vessel is equipped with hydrochloric acid storage tank, and the dilute hydrochloric acid for adjusting pH value in first order enzymatic vessel is equipped in hydrochloric acid storage tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820282020.6U CN208071710U (en) | 2018-02-28 | 2018-02-28 | Insulation construction in three enzymes, one ferment treatment solution production system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820282020.6U CN208071710U (en) | 2018-02-28 | 2018-02-28 | Insulation construction in three enzymes, one ferment treatment solution production system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208071710U true CN208071710U (en) | 2018-11-09 |
Family
ID=64039611
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201820282020.6U Active CN208071710U (en) | 2018-02-28 | 2018-02-28 | Insulation construction in three enzymes, one ferment treatment solution production system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208071710U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109810874A (en) * | 2019-03-27 | 2019-05-28 | 深圳职业技术学院 | A kind of biology enzymatic reaction system |
CN113278507A (en) * | 2021-05-07 | 2021-08-20 | 谢长安 | Constant temperature ventilation defoaming type food fermentation vat |
-
2018
- 2018-02-28 CN CN201820282020.6U patent/CN208071710U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109810874A (en) * | 2019-03-27 | 2019-05-28 | 深圳职业技术学院 | A kind of biology enzymatic reaction system |
CN113278507A (en) * | 2021-05-07 | 2021-08-20 | 谢长安 | Constant temperature ventilation defoaming type food fermentation vat |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN208071710U (en) | Insulation construction in three enzymes, one ferment treatment solution production system | |
CN202909140U (en) | Frequency-conversion-controlled energy-saving continuous sterilization system | |
CN101724551B (en) | Full mixed anaerobic reaction circulating device and circulating method for methane reaction raw materials | |
CN110656043A (en) | Microbial fermentation tank for producing liquid feed additive | |
CN207109009U (en) | A kind of royal jelly enzymolysis experimental provision | |
CN108203684A (en) | The production system and method for a kind of rich micro- Nattokinase of three enzymes, one ferment | |
CN110656044A (en) | Novel intelligent microbial fermentation device | |
CN208071687U (en) | A kind of production system of the rich micro- Nattokinase of three enzymes, one ferment | |
CN208023027U (en) | Insulation construction in three enzymes, one ferment richness microorganism liquid production system | |
CN207828227U (en) | Honey wine brewing ferment at constant temperature equipment | |
CN208023030U (en) | The production that three enzymes, one ferment eats medicinal fungus bacterium peptide feeds intake structure | |
CN204224599U (en) | Modified version enzymatic vessel is used in the preparation of Testa Tritici xylo-oligosaccharide enzyme process | |
CN207828289U (en) | A kind of microbial solid fermentation tank | |
CN208362332U (en) | A kind of animal nutrition fermentor | |
CN109337800A (en) | A kind of hydrolysis acidification and anaerobic fermentation integrated device | |
CN207002704U (en) | A kind of two-chamber fermentation tank | |
CN205635620U (en) | Biogas fermentation system | |
CN208023028U (en) | Cleaning device in three enzymes, one ferment selenium-rich Antrodia camphorata micromolecular polysaccharide production system | |
CN208071711U (en) | Cleaning device in the rich micro- radix fici simplicissimae micromolecular polysaccharide production system of three enzymes, one ferment | |
CN209438582U (en) | A kind of preparation facilities of anti-chamotte mould polycarboxylate water-reducer | |
CN207786587U (en) | A kind of sulfamate high-effective water-reducing agent is without heat source response system | |
CN205954016U (en) | Yeast self -dissolving equipment | |
CN207608499U (en) | A kind of biological organic fertilizer fermentation vat | |
CN216073816U (en) | Bacillus coagulans fermentation tank | |
CN208055348U (en) | A kind of air source heat pump firedamp gas equipment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |