CN217438193U - Energy-saving continuous enzyme reaction device - Google Patents

Energy-saving continuous enzyme reaction device Download PDF

Info

Publication number
CN217438193U
CN217438193U CN202123241065.XU CN202123241065U CN217438193U CN 217438193 U CN217438193 U CN 217438193U CN 202123241065 U CN202123241065 U CN 202123241065U CN 217438193 U CN217438193 U CN 217438193U
Authority
CN
China
Prior art keywords
enzyme reaction
water conservancy
conservancy diversion
ring
reaction tank
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
Application number
CN202123241065.XU
Other languages
Chinese (zh)
Inventor
于海勤
庞保航
于汭
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong Ruizhi Pharmaceutical Technology Co ltd
Original Assignee
Shandong Ruizhi Pharmaceutical Technology Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shandong Ruizhi Pharmaceutical Technology Co ltd filed Critical Shandong Ruizhi Pharmaceutical Technology Co ltd
Priority to CN202123241065.XU priority Critical patent/CN217438193U/en
Application granted granted Critical
Publication of CN217438193U publication Critical patent/CN217438193U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Landscapes

  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

The utility model relates to an enzyme reaction device, in particular to an energy-saving continuous enzyme reaction device. The energy-saving continuous enzyme reaction device comprises an enzyme reaction tank group, wherein the enzyme reaction tank group is formed by connecting a plurality of reaction tank bodies in series, and is characterized in that: the internal water conservancy diversion frame that is equipped with of retort, water conservancy diversion frame include suitable for reading ring sum suitable for reading ring, are connected with a plurality of water conservancy diversion spouts between suitable for reading ring sum suitable for reading ring, are equipped with the water conservancy diversion bucket in the water conservancy diversion frame, and on the water conservancy diversion bucket end opening was fixed in the end opening ring, on the water conservancy diversion bucket end opening was fixed in hollow ring, the outer edge of hollow ring installed the locating piece that corresponds the water conservancy diversion spout. The utility model has the advantages that: the feed liquid is circulated inside and outside the guide barrel, the stirring and mixing effects are generated, the feed liquid is fully mixed, the catalytic efficiency is improved, and the power consumption is reduced; the upper liquid level of the guide barrel is always consistent with that of the reaction tank body, so that the mixing effect is prevented from being influenced by turbulence.

Description

Energy-saving continuous enzyme reaction device
(I) technical field
The utility model relates to an enzyme reaction device, in particular to an energy-saving continuous enzyme reaction device.
(II) background of the invention
The enzyme reaction is a reaction taking enzyme as a catalyst, and the enzyme and a substrate are fully mixed in a reaction device in the catalytic reaction process to generate a target product through catalysis. With the rapid development of biotechnology, bio-enzyme reactions are increasingly being applied to industrial production. The existing enzyme reaction device adopts high-power stirring equipment during working, so that the power cost is greatly improved; dead angles are easily generated in the stirring and mixing process, and the working efficiency of the device is influenced; the stirring and mixing device is easy to generate noise and has influence on the environment; the inside of the device is inconvenient to clean, and some substances are easy to adhere to the inner wall of the device to influence the use of the device.
Disclosure of the invention
The utility model discloses a remedy prior art not enough, provide a feed liquid and mix abundant, catalysis efficiency is high, power consumption is few, no vortex produces, the energy-saving continuous enzyme reaction unit that the energy consumption is low.
The utility model discloses a realize through following technical scheme:
the utility model provides an energy-saving continuous enzyme reaction unit, includes enzyme reaction jar group, and enzyme reaction jar group is by a plurality of retort body series connection, characterized by: the reactor is characterized in that a flow guide frame is arranged in the reactor body and comprises an upper opening ring and a lower opening ring, a plurality of flow guide chutes are connected between the upper opening ring and the lower opening ring, a flow guide barrel is arranged in the flow guide frame, the lower opening of the flow guide barrel is fixed on the lower opening ring, the upper opening of the flow guide barrel is fixed on the hollow ring, and a positioning block corresponding to the flow guide chutes is arranged on the outer edge of the hollow ring.
A guide plate is arranged under the guide frame.
The bottom of the reaction tank body is connected with a circulating pump through a material suction pipe, and the circulating pump is connected to the lower part of the flow guide barrel through a material discharge pipe.
The head end of the enzyme reaction tank group is connected with the counter-flow heat exchanger through a new feed liquid outlet, and the tail end of the enzyme reaction tank group is connected with the counter-flow heat exchanger through an enzyme reaction liquid inlet.
The countercurrent heat exchanger is respectively connected with a new feed liquid inlet and an enzyme reaction liquid outlet.
The utility model has the advantages that: the feed liquid is circulated inside and outside the guide barrel, the stirring and mixing effects are generated, the feed liquid is fully mixed, the catalytic efficiency is improved, and the power consumption is reduced; the upper liquid level of the guide barrel is always consistent with the upper liquid level of the reaction tank body, so that the mixing effect is prevented from being influenced by turbulence; the counter-flow exchanger is used for recycling cold and hot energy, and the effects of energy conservation and consumption reduction are obvious.
(IV) description of the drawings
The present invention will be further described with reference to the accompanying drawings.
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic view of the mounting structure of the positioning block and the guide chute of the present invention;
in the figure, 1 enzyme reaction tank group, 2 reaction tank body, 3 diversion frame, 4 upper opening circular ring, 5 lower opening circular ring, 6 diversion chute, 7 diversion barrel, 8 hollow circular ring, 9 positioning block, 10 diversion plate, 11 material suction pipe, 12 circulating pump, 13 material discharge pipe, 14 new feed liquid outlet, 15 counter-current heat exchanger, 16 enzyme reaction liquid inlet, 17 new feed liquid inlet, 18 enzyme reaction liquid outlet.
(V) detailed description of the preferred embodiments
The attached drawing is a concrete embodiment of the utility model. This embodiment includes enzyme reaction jar group 1, enzyme reaction jar group 1 is by a plurality of retort body 2 series connection, be equipped with water conservancy diversion frame 3 in the retort body 2, water conservancy diversion frame 3 includes suitable for reading ring 4 and lower mouthful ring 5, be connected with a plurality of water conservancy diversion spouts 6 between suitable for reading ring 4 and the lower mouthful ring 5, be equipped with water conservancy diversion bucket 7 in the water conservancy diversion frame 3, on water conservancy diversion bucket 7 lower port was fixed in lower mouthful ring 5, on water conservancy diversion bucket 7 upper port was fixed in hollow ring 8, hollow ring 8 is outer along installing the locating piece 9 that corresponds water conservancy diversion spout 6. A guide plate 10 is arranged under the guide frame 3. The bottom of the reaction tank body 2 is connected with a circulating pump 12 through a material suction pipe 11, and the circulating pump 12 is connected with the lower part of the guide flow barrel 7 through a material discharge pipe 13. The head end of the enzyme reaction tank group 1 is connected with a counter-flow heat exchanger 15 through a new feed liquid outlet 14, and the tail end of the enzyme reaction tank group 1 is connected with the counter-flow heat exchanger 15 through an enzyme reaction liquid inlet 16. The counter-current heat exchanger 15 is connected with a new feed liquid inlet 17 and an enzyme reaction liquid outlet 18 respectively.
Adopt the utility model discloses an energy-saving continuous enzyme reaction unit, water conservancy diversion frame 3 is cylindricly, and the centre of suitable for reading ring 4 and suitable for reading ring 5 is connected with 4-8 vertical arrangement, equidistant distribution's water conservancy diversion spouts 6, settles and put in 2 central points of the retort body. The guide barrel 7 is a round barrel-shaped object made of flexible materials such as non-woven fabrics, the diameter of the guide barrel is close to the inner diameter of the guide frame 3, the lower opening is tightly fixed on the lower opening ring 5, and the upper opening is tightly fixed on the hollow ring 8. The hollow circular ring 8 is made of light materials, the outer diameter of the hollow circular ring is slightly smaller than the inner diameter of the flow guide frame 3, 4-8 positioning blocks 9 are installed on the outer edge of the hollow circular ring 8, and the positioning blocks 9 are correspondingly embedded in the flow guide sliding grooves 6 on the flow guide frame 3. The guide plate 10 is arranged right below the guide frame 3; the circulating pump 12 is connected with the bottom of the reaction tank body 2 through a material suction pipe 11, and a material discharge pipe 13 is arranged at the middle lower part of the guide barrel 7. The circulating pump 12 sucks feed liquid from the reaction tank body 2, the discharge pipe 13 generates upward vertical jet flow near the bottom of the guide flow barrel 7, the feed liquid around and at the bottom is driven to move upwards along the guide flow barrel 7, the feed liquid enters the space between the guide flow barrel 7 and the reaction tank body 2 after reaching the upper opening and moves downwards, a part of the feed liquid enters the circulating pump 12 to form new jet flow after reaching the bottom under the action of the guide plate 10, and a part of the feed liquid enters the bottom of the guide flow barrel 7 and is pushed by the jet flow to continue to move upwards, so that the feed liquid forms circulation inside and outside the guide flow barrel 7, and stirring and mixing effects are generated. The hollow ring 8 can float up and down along the direction of the diversion chute 6 by means of the buoyancy of the liquid surface, and simultaneously drives the upper opening of the diversion barrel 7 to move, so that the liquid surface of the diversion barrel 7 is always consistent with the outer liquid surface. The new feed liquid flows through the counter-flow heat exchanger 15 at a constant speed, exchanges heat or cold with enzyme reaction liquid which comes from the tail end of the enzyme reaction tank group 1 and completes catalytic reaction, and then enters the head end of the enzyme reaction tank group 1 to start enzyme reaction; simultaneously, feed liquid at the head end of the enzyme reaction tank group 1 flows into the second reaction tank body 2 at a constant speed, and the feed liquid sequentially flows into the tail end of the enzyme reaction tank group 1 to complete enzyme reaction; finally, the enzyme reaction liquid enters a counter-current heat exchanger 15 to transfer heat or cold to new feed liquid, and the enzyme reaction stage is finished and the next procedure is carried out.

Claims (5)

1. The utility model provides an energy-saving continuous enzyme reaction unit, includes enzyme reaction jar group (1), and enzyme reaction jar group (1) is by a plurality of retort body (2) series connection, characterized by: be equipped with water conservancy diversion frame (3) in retort body (2), water conservancy diversion frame (3) are connected with a plurality of water conservancy diversion spouts (6) including suitable for reading ring (4) and suitable for reading ring (5) between suitable for reading ring (4) and suitable for reading ring (5) down, be equipped with water conservancy diversion bucket (7) in water conservancy diversion frame (3), on water conservancy diversion bucket (7) end opening was fixed in end opening ring (5), water conservancy diversion bucket (7) are suitable for reading and are fixed in on hollow ring (8), locating piece (9) that correspond water conservancy diversion spout (6) are installed along installing outward to hollow ring (8).
2. The continuous enzyme reaction apparatus according to claim 1, wherein: a guide plate (10) is arranged under the guide frame (3).
3. The continuous enzyme reaction apparatus according to claim 1, wherein: the bottom of the reaction tank body (2) is connected with a circulating pump (12) through a material suction pipe (11), and the circulating pump (12) is connected to the lower part of the diversion barrel (7) through a material discharge pipe (13).
4. The continuous enzyme reaction apparatus according to claim 1, wherein: the head end of the enzyme reaction tank group (1) is connected with a counter-flow heat exchanger (15) through a new feed liquid outlet (14), and the tail end of the enzyme reaction tank group (1) is connected with the counter-flow heat exchanger (15) through an enzyme reaction liquid inlet (16).
5. The continuous enzyme reaction apparatus according to claim 4, wherein: the counter-current heat exchanger (15) is respectively connected with a new feed liquid inlet (17) and an enzyme reaction liquid outlet (18).
CN202123241065.XU 2021-12-22 2021-12-22 Energy-saving continuous enzyme reaction device Active CN217438193U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202123241065.XU CN217438193U (en) 2021-12-22 2021-12-22 Energy-saving continuous enzyme reaction device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202123241065.XU CN217438193U (en) 2021-12-22 2021-12-22 Energy-saving continuous enzyme reaction device

Publications (1)

Publication Number Publication Date
CN217438193U true CN217438193U (en) 2022-09-16

Family

ID=83209509

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202123241065.XU Active CN217438193U (en) 2021-12-22 2021-12-22 Energy-saving continuous enzyme reaction device

Country Status (1)

Country Link
CN (1) CN217438193U (en)

Similar Documents

Publication Publication Date Title
CN203904338U (en) Double-path reflux anaerobic reaction system and reactor for producing biogas by using straw
CN201908001U (en) Novel jet aerator
CN104759228B (en) Gas push formula is from stirring combination purification groove
CN201241138Y (en) Combined fermentation pot
CN201376917Y (en) Solid liquid flow mixing device of anaerobic reactor
CN101508486B (en) Anaerobic reactor tridimensional flow agitating apparatus
CN217438193U (en) Energy-saving continuous enzyme reaction device
CN201817478U (en) Marsh gas reaction vessel
CN216106232U (en) Rural sewage treatment plant of low energy consumption
CN2550372Y (en) Double circulation gas stirring anaerobic fermentation tank
CN203833929U (en) Complete mixed anaerobic bioreactor
CN106669570B (en) One kind tiltedly arranging pre-heated chemical reaction kettle
CN103103215B (en) Gradient circulation stirring method in marsh gas reactor and anaerobic reactor thereof
CN111204789A (en) Calcium carbonate carbonizing apparatus
CN201581073U (en) Full-automatic two-step multi-stage fermentation methane tank
CN110643492B (en) Material stirring device and method for producing biogas through anaerobic fermentation
CN213012822U (en) Circulation anaerobic fermentation tank
CN204619874U (en) Gas push formula is from stirring combination purification groove
CN205062077U (en) Gas -liquid jointly stirs venturi - entirely and mixes anaerobic digestion reactor
CN209039079U (en) A kind of calcium carbonate carbonizing plant
CN107051353B (en) A kind of cycling stirring type chemical reaction kettle
CN106582484B (en) A kind of cycling stirring type chemical reaction kettle
CN106669571B (en) A kind of tiltedly row's formula stirring chemical reaction kettle
CN203319762U (en) Self-circulation anaerobic reactor
CN208166662U (en) A kind of aerobic particle mud continuous flow type reactor

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant