CN204509277U - A kind of hydrate concentrates enzyme liquid device - Google Patents
A kind of hydrate concentrates enzyme liquid device Download PDFInfo
- Publication number
- CN204509277U CN204509277U CN201520103417.0U CN201520103417U CN204509277U CN 204509277 U CN204509277 U CN 204509277U CN 201520103417 U CN201520103417 U CN 201520103417U CN 204509277 U CN204509277 U CN 204509277U
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- enzyme liquid
- basin
- reactor
- hydrate
- separating machine
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Abstract
A kind of hydrate concentrates enzyme liquid device, comprise the reactor, the separating machine Sum decomposition still that connect successively, the opening for feed of described reactor is connected with rare enzyme liquid basin, the discharge port of separating machine is connected with dense enzyme liquid basin, the discharge port of decomposing pot is connected with water basin, described decomposing pot is also connected with gas holder tank, and gas holder tank is communicated with water basin with reactor respectively.The utility model structure is simple, and very little on enzymic activity impact, running cost is low, energy-conservation saving simultaneously, economic environmental protection.
Description
Technical field
The utility model relates to concentrating and separating technical field, particularly relates to a kind of device utilizing hydrate to concentrate enzyme liquid.
Background technology
Enzyme liquid concentrating and separating method traditional at present mainly comprises membrane sepn, salting-out separation, evaporation concentration and freeze concentration etc.But these methods all exist respective problem in actual applications, such as, the mould material price of membrane sepn is higher, regeneration rate is low, fouling membrane and concentration polarization phenomenon are comparatively serious, have impact on the life-span of film, adds investment cost; The foreign matter content of salting-out separation is higher, easily causes the deactivation of enzyme, and produces more sewage; Evaporation concentration efficiency is low, and facility investment is large, and energy consumption is high; Freeze concentration is due to the constraint by phase balance condition, and thickening efficiency is low.Therefore in order to energy efficient, raising separation and concentration efficiency, need to continually develop new environmentally friendly enzyme liquid concentrating and separating method.
Hydrate soln isolation technique is considered to the new technology that can substitute tradition evaporation, cold method, this technology can be carried out on the freezing point temperature of water, can reduce the energy consumption of solution separating process, be a kind of new technique of the simple and environmental protection of technique, and obtain and pay close attention to widely.Existing hydrate separation technology is mainly used in the aspect such as sea water desaltination, gas delivery, and in enzyme liquid concentrates, there is not been reported.
Utility model content
The purpose of this utility model is the concentrating unit providing a kind of low cost, less energy-consumption for enzyme liquid.
For achieving the above object, the technical scheme that the utility model proposes is:
A kind of hydrate concentrates enzyme liquid device, comprise the reactor, the separating machine Sum decomposition still that connect successively, the opening for feed of described reactor is connected with rare enzyme liquid basin, the discharge port of separating machine is connected with dense enzyme liquid basin, the discharge port of decomposing pot is connected with water basin, described decomposing pot is also connected with gas holder tank, and gas holder tank is communicated with water basin with reactor respectively.
In the utility model, the gas produced in described decomposing pot, by gas holder tank, leads to reactor, and described reactor, separating machine, decomposing pot and gas holder tank form gas circulation and utilize loop.
In the utility model, described rare enzyme liquid basin, dense enzyme liquid basin and water basin are atmospheric storage tank, and gas holder tank is pressure storage tank, and the gas for reactor enters provides necessary high pressure.
In the utility model, described reactor Sum decomposition still is high-tension apparatus, and maximum working pressure 25MPa, is provided with chuck outside still, and the chuck of described reactor is connected with the cooling fluid of cooling, and the chuck of described decomposing pot is connected with the heating fluid of intensification.
In the utility model, described separating machine is high pressure low temperature separating device, can select high pressure low temperature whizzer or filter.
Further, operating pressure and the temperature of described reactor and separating machine are identical, ensure that solid phase hydration thing does not decompose in advance.
Compared with prior art, the utility model has the advantage of:
(1) gas circulation utilizes, and gas and rare enzyme liquid form hydrate under certain condition, and hydrate generates gas and water after decomposing, and gas can return reactor and again be utilized, and effects of energy saving and emission reduction is good;
(2) water recoverable, the water that decomposition of hydrate produces can be back to spice or the fermentation workshop section of enzyme production, saving water resource;
(3) technological process is close to normal temperature, and very little on enzymic activity impact, enzyme liquid still can keep very high reactivity, and energy consumption is little, and thickening efficiency is high;
(4) Production Flow Chart is simple, and can realize operate continuously, energy consumption is little, and running cost is low, economic environmental protection.
Accompanying drawing explanation
Fig. 1 is flowage structure schematic diagram of the present utility model.
In figure: rare enzyme liquid basin 1, reactor 2, separating machine 3, dense enzyme liquid basin 4, decomposing pot 5, water basin 6, gas holder tank 7.
Embodiment
Below in conjunction with Figure of description and concrete preferred embodiment, the utility model is further described, but does not therefore limit protection domain of the present utility model.
Hydrate shown in Figure 1 concentrates enzyme liquid device, comprise rare enzyme liquid basin 1, reactor 2, separating machine 3, dense enzyme liquid basin 4, decomposing pot 5, water basin 6 and gas holder tank 7, the opening for feed of described reactor 2 connects rare enzyme liquid basin 1, the discharge port of reactor 2 connects separating machine, the opening for feed of decomposing pot 5 connects separating machine 3, the discharge port of decomposing pot 5 connects water basin 6, separating machine 3 is also connected with dense enzyme liquid basin 4, gas holder tank 7 also distinguishes ligation still 2 Sum decomposition still 5, and the sewage draining exit of gas holder tank 7 is communicated with water basin 6.
Hydrate described in the utility model concentrates enzyme liquid device and is applied to enzyme liquid when concentrating, rare enzyme liquid flows into reactor 2 in rare enzyme liquid basin 1, the recycle gas passed into gas holder tank 7 reacts under high pressure low temperature, the hydrate generated flows in separating machine 3, through the solid-liquid separation of separating machine 3, it is for subsequent use that liquid phase is that dense enzyme liquid passes in dense enzyme liquid basin 4, solid phase is sent in decomposing pot 5, thermal degradation is gas and liquid water, gas enters to recycle in gas holder tank 7, and water flows in water basin 6 with for subsequent use.
In above process, gas circulation utilizes, and water is recoverable also, and whole flow process is very little to the activity influence of enzyme, energy-conservation saving, economic environmental protection.
Claims (3)
1. a hydrate concentrates enzyme liquid device, it is characterized in that, comprise the reactor, the separating machine Sum decomposition still that connect successively, the opening for feed of described reactor is connected with rare enzyme liquid basin, the discharge port of separating machine is connected with dense enzyme liquid basin, the discharge port of decomposing pot is connected with water basin, and described decomposing pot is also connected with gas holder tank, and gas holder tank is communicated with water basin with reactor respectively.
2. hydrate according to claim 1 concentrates enzyme liquid device, it is characterized in that, described rare enzyme liquid basin, dense enzyme liquid basin and water basin are atmospheric storage tank, and gas holder tank is pressure storage tank; Described reactor, separating machine Sum decomposition still are high-tension apparatus.
3. hydrate according to claim 1 concentrates enzyme liquid device, it is characterized in that, is provided with chuck outside the still of described reactor Sum decomposition still, and the chuck of described reactor is connected with the cooling fluid of cooling, and the chuck of described decomposing pot is connected with the heating fluid of intensification.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520103417.0U CN204509277U (en) | 2015-02-13 | 2015-02-13 | A kind of hydrate concentrates enzyme liquid device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520103417.0U CN204509277U (en) | 2015-02-13 | 2015-02-13 | A kind of hydrate concentrates enzyme liquid device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204509277U true CN204509277U (en) | 2015-07-29 |
Family
ID=53707271
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520103417.0U Expired - Fee Related CN204509277U (en) | 2015-02-13 | 2015-02-13 | A kind of hydrate concentrates enzyme liquid device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204509277U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110050914A (en) * | 2018-12-24 | 2019-07-26 | 广东省农业科学院蚕业与农产品加工研究所 | A kind of electric field-assisted improves the method and device of hydrate inspissated juice quality |
-
2015
- 2015-02-13 CN CN201520103417.0U patent/CN204509277U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110050914A (en) * | 2018-12-24 | 2019-07-26 | 广东省农业科学院蚕业与农产品加工研究所 | A kind of electric field-assisted improves the method and device of hydrate inspissated juice quality |
| CN110050914B (en) * | 2018-12-24 | 2022-05-13 | 广东省农业科学院蚕业与农产品加工研究所 | Method and device for improving quality of hydrate concentrated juice with assistance of electric field |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150729 Termination date: 20170213 |