CN207062259U - A kind of novel saccharification tank - Google Patents

A kind of novel saccharification tank Download PDF

Info

Publication number
CN207062259U
CN207062259U CN201720953598.5U CN201720953598U CN207062259U CN 207062259 U CN207062259 U CN 207062259U CN 201720953598 U CN201720953598 U CN 201720953598U CN 207062259 U CN207062259 U CN 207062259U
Authority
CN
China
Prior art keywords
feed pipe
novel
tank according
recycle feed
saccharification 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.)
Expired - Fee Related
Application number
CN201720953598.5U
Other languages
Chinese (zh)
Inventor
朱凤杰
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.)
Beijing Guangsheng Source Biotechnology Co Ltd
Original Assignee
Beijing Guangsheng Source Biotechnology 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 Beijing Guangsheng Source Biotechnology Co Ltd filed Critical Beijing Guangsheng Source Biotechnology Co Ltd
Priority to CN201720953598.5U priority Critical patent/CN207062259U/en
Application granted granted Critical
Publication of CN207062259U publication Critical patent/CN207062259U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

Glucose syrup manufacturing equipment field is the utility model is related to, more particularly to a kind of novel saccharification tank.It includes housing, and saccharification chamber is provided with the housing, and circulation discharge nozzle and recycle feed pipe are provided with the housing, and the circulation discharge nozzle connects the saccharification chamber with the recycle feed pipe;Electric heater is installed between the circulation discharge nozzle and the recycle feed pipe;Elevator pump is installed on the circulation discharge nozzle;The housing is provided with charging aperture and discharging opening.The purpose of this utility model is to provide a kind of novel saccharification tank, to solve the problems, such as existing saccharifying tank mode of heating existing defects.

Description

A kind of novel saccharification tank
Technical field
Glucose syrup manufacturing equipment field is the utility model is related to, more particularly to a kind of novel saccharification tank.
Background technology
Saccharification is process important in glucose syrup production process, directly influences the quality and yield of final products, sugar Change is carried out in saccharifying tank.
Appropriate standard carbohydrase is added in saccharifying tank, after being incubated a period of time, enzyme deactivation can be carried out;Enzyme deactivation process need by Temperature is raised to 80 degree or so, and enzyme deactivation process needs to heat slurries, by the temperature of slurries by 60 degree or so liftings to 80 degree or so; Traditional saccharifying tank is the saccharification reaction vessel of a transition nature, and the high temperature enzyme deactivation after saccharification is usually to be changed using board-like Hot device heats liquid glucose, and high-temperature water vapor is either filled with into saccharifying tank or hot coil is installed in saccharifying tank.Three of the above side There is a certain degree of deficiency during specifically used, first way uses in plate type heat exchanger heating process formula, Coherency albumen in saccharified liquid can be attached on the inside of plate type heat exchanger in deformation process, not only reduce heat transfer effect, simultaneously Also flow is reduced, it is necessary to often unpick and wash, and increases workload;Substantial amounts of high-temperature vapor is filled with second way saccharifying tank to drop The concentration of low sugar liquid, increases the dosage of the steam raising of subsequent concentration syrup process, and due to tank body volume itself it is big, it is necessary to The liquid glucose needs that integrally heat up is filled with substantial amounts of steam, and then larger air pressure can be caused to impact to tank body, be easily damaged tank body, High also is required to the overall tightness of tank body, adds operation cost;The third mode in use, although coil pipe can Increase liquid glucose heating surface, but itself bending coiling be immersed in liquid glucose, liquid glucose is easily attached on coil pipe, and is leaned on The local liquid glucose of nearly coil pipe is heated most fast, and the coherency albumen in saccharified liquid can also adhere to coil pipe, Er Qiepan in deformation process Pipe cleaning trouble, can increase additional workload.
Utility model content
The purpose of this utility model is to provide a kind of novel saccharification tank, to solve existing saccharifying tank mode of heating in the presence of scarce The problem of falling into.
The purpose of this utility model is realized by following technical proposals:
A kind of novel saccharification tank, it includes housing, and saccharification chamber is provided with the housing, is provided with and recycles on the housing Expects pipe and recycle feed pipe, the circulation discharge nozzle connect the saccharification chamber with the recycle feed pipe;The circulation discharge nozzle Electric heater is installed between the recycle feed pipe;Elevator pump is installed on the circulation discharge nozzle;The housing is provided with Charging aperture and discharging opening.
Further, the recycle feed pipe has a two or more, and each recycle feed pipe is along the housing circumferencial direction It is evenly arranged.
Further, the recycle feed tube end is provided with jet pipe.
Further, there is a upward angle in the nozzle exit direction.
Further, the recycle feed pipe is arranged at the circulation discharge nozzle bottom.
Further, the hull outside is provided with heat-insulation layer.
Further, the heat-insulation layer is polyurethane insulation coating.
Further, the saccharification intracavitary is provided with temperature sensor, the temperature sensor, the electric heater respectively with Central processing unit electrically connects.
Further, the temperature sensor is GG-K-30 Series Temperature Transmitters.
Further, the central processing unit is IST200 central series processors.
The utility model has the following advantages that compared with prior art:
1. novel saccharification tank described in the utility model, it includes housing, is provided with saccharification chamber in the housing, on the housing Circulation discharge nozzle and recycle feed pipe are installed, the circulation discharge nozzle connects the saccharification chamber with the recycle feed pipe;Institute State and electric heater is installed between circulation discharge nozzle and the recycle feed pipe;Elevator pump is installed on the circulation discharge nozzle;Choosing With such a mode of heating, it is not necessary to high-temperature steam is poured into saccharifying tank, and slurries flow fast through electrical heating in heating process Device, coherency albumen and slurries in slurries are not easy to paste on electric heater in itself;In saccharifying, slurries pass through continuous Circulation, plays a part of stirring, can promote being sufficiently mixed for slurries and carbohydrase.
2. recycle feed tube end described in the utility model is provided with jet pipe, jet pipe can increase into saccharification intracavitary slurries Flow velocity, promote saccharification intracavitary slurries flowing.
3. saccharification intracavitary described in the utility model is provided with temperature sensor, the temperature sensor, the electric heater point Do not electrically connected with central processing unit;Temperature sensor monitors the temperature of saccharification intracavitary slurries in real time, during temperature signal is delivered to Central processor, central processing unit contrast slurry temperature and design temperature, signal is transmitted to electric heater, adjusts adding for electric heater Thermal power, realize automatically adjusting for slurry temperature.
4. hull outside described in the utility model is provided with heat-insulation layer;Saccharifying tank radiating is reduced, reduces energy resource consumption.
Brief description of the drawings
Fig. 1 is novel saccharification jar structure figure described in the utility model;
Fig. 2 is the utility model electrical connection diagram;
In figure:1- housings, 2- charging apertures, 3- heat-insulation layers, 4- temperature sensors, 5- saccharification chamber, 6- circulations discharge nozzle, 7- are carried Rise pump, 8- electric heaters, 9- recycle feeds pipe, 10- discharging openings, 11- jet pipes.
Embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with accompanying drawing, it is clear that described Embodiment is the utility model part of the embodiment, rather than whole embodiments.Based on the embodiment in the utility model, sheet The every other embodiment that field those of ordinary skill is obtained under the premise of creative work is not made, belongs to this practicality Novel protected scope.
, it is necessary to explanation in description of the present utility model, term " " center ", " on ", " under ", it is "left", "right", " perpendicular Directly ", the orientation of the instruction such as " level ", " interior ", " outer " or position relationship are based on orientation shown in the drawings or position relationship, are only Described for the ease of description the utility model and simplifying, rather than instruction or imply signified device or element must have it is specific Orientation, with specific azimuth configuration and operation, therefore it is not intended that to limitation of the present utility model.In addition, term " the One ", " second ", " the 3rd " are only used for describing purpose, and it is not intended that instruction or hint relative importance.
, it is necessary to which explanation, unless otherwise clearly defined and limited, term " are pacified in description of the present utility model Dress ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or integratedly Connection;Can be mechanical connection or electrical connection;Can be joined directly together, can also be indirectly connected by intermediary, It can be the connection of two element internals.For the ordinary skill in the art, above-mentioned art can be understood with concrete condition Concrete meaning of the language in the utility model.
Referring to Fig. 1, a kind of novel saccharification tank, it includes housing 1, and saccharification chamber 5 is provided with housing 1, is provided with and follows on housing 1 Ring discharge nozzle 6 and recycle feed pipe 9, circulation discharge nozzle 6 connect saccharification chamber 5 with recycle feed pipe 9;Circulate discharge nozzle 6 and circulation Electric heater 8 is installed between feed pipe 9;Elevator pump 7 is installed on circulation discharge nozzle 6;Housing 1 is provided with charging aperture 2 and discharging Mouth 10;From such a mode of heating, it is not necessary to high-temperature steam is poured into saccharifying tank, and slurries flow fast through in heating process Electric heater 8, coherency albumen and slurries in slurries are not easy to paste on electric heater 8 in itself;In saccharifying, slurries By constantly circulating, play a part of stirring, being sufficiently mixed for slurries and carbohydrase can be promoted.
Referring to Fig. 1, recycle feed pipe 9 has two or more, and each recycle feed pipe 9 is evenly arranged along the circumferencial direction of housing 1;Follow The end of ring feed pipe 9 is provided with jet pipe 11;The export direction of jet pipe 11 has a upward angle;Slurries are formed in saccharification chamber 5 Turbulence Flow, promote being sufficiently mixed for slurries, prevent slurries from precipitating so that concentration of slurry is uniform.
Referring to Fig. 1, recycle feed pipe 9 is arranged at circulation discharge nozzle 6 bottom;Flowing can rapidly for the slurries of saccharification chamber 5 bottom To drive the slurries on saccharification chamber 5 top to flow, lower slurry concentration is larger under normal circumstances, more needs the slurries liquid stream of high speed Impact, and then form Turbulence Flow.
Referring to Fig. 1, the outside of housing 1 is provided with heat-insulation layer 3;Saccharifying tank radiating is reduced, reduces energy resource consumption;Heat-insulation layer 3 is poly- Urethane heat-insulation layer;Polyurethane insulation coating has the advantages that specific strength is high, thermal conductivity factor is small.
Referring to Fig. 1, Fig. 2, be provided with temperature sensor 4 in saccharification chamber 5, temperature sensor 4, electric heater 8 respectively with center Processor electrically connects;Temperature sensor 4 is GG-K-30 Series Temperature Transmitters;The central processing unit is in IST200 series Central processor;The temperature of slurries, central processing unit is delivered to by temperature signal in the chamber 5 of monitoring saccharification in real time of temperature sensor 4, in Central processor contrasts slurry temperature and design temperature, and it is real to electric heater 8, the heating power of regulation electric heater 8 to transmit signal Existing slurry temperature automatically adjusts.
Finally it should be noted that:Various embodiments above is only to illustrate the technical solution of the utility model, rather than it is limited System;Although the utility model is described in detail with reference to foregoing embodiments, one of ordinary skill in the art should Understand:It can still modify to the technical scheme described in foregoing embodiments, either to which part or whole Technical characteristic carries out equivalent substitution;And these modifications or replacement, the essence of appropriate technical solution is departed from this practicality newly The scope of each embodiment technical scheme of type.

Claims (10)

  1. A kind of 1. novel saccharification tank, it is characterised in that:Saccharification chamber is provided with including housing, in the housing, is installed on the housing There are circulation discharge nozzle and recycle feed pipe, the circulation discharge nozzle connects the saccharification chamber with the recycle feed pipe;It is described to follow Electric heater is installed between ring discharge nozzle and the recycle feed pipe;Elevator pump is installed on the circulation discharge nozzle;The shell Body is provided with charging aperture and discharging opening.
  2. 2. novel saccharification tank according to claim 1, it is characterised in that:The recycle feed pipe has two or more, each institute Recycle feed pipe is stated to be evenly arranged along the housing circumferencial direction.
  3. 3. novel saccharification tank according to claim 1, it is characterised in that:The recycle feed tube end is provided with jet pipe.
  4. 4. novel saccharification tank according to claim 3, it is characterised in that:There is a upward angle in the nozzle exit direction Degree.
  5. 5. novel saccharification tank according to claim 1, it is characterised in that:The recycle feed pipe is arranged at described recycle Expects pipe bottom.
  6. 6. novel saccharification tank according to claim 1, it is characterised in that:The hull outside is provided with heat-insulation layer.
  7. 7. novel saccharification tank according to claim 6, it is characterised in that:The heat-insulation layer is polyurethane insulation coating.
  8. 8. novel saccharification tank according to claim 1, it is characterised in that:The saccharification intracavitary is provided with temperature sensor, institute State temperature sensor, the electric heater electrically connects with central processing unit respectively.
  9. 9. novel saccharification tank according to claim 8, it is characterised in that:The temperature sensor is GG-K-30 series temperature Spend sensor.
  10. 10. novel saccharification tank according to claim 8, it is characterised in that:The central processing unit is in IST200 series Central processor.
CN201720953598.5U 2017-08-01 2017-08-01 A kind of novel saccharification tank Expired - Fee Related CN207062259U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720953598.5U CN207062259U (en) 2017-08-01 2017-08-01 A kind of novel saccharification tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720953598.5U CN207062259U (en) 2017-08-01 2017-08-01 A kind of novel saccharification tank

Publications (1)

Publication Number Publication Date
CN207062259U true CN207062259U (en) 2018-03-02

Family

ID=61518715

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720953598.5U Expired - Fee Related CN207062259U (en) 2017-08-01 2017-08-01 A kind of novel saccharification tank

Country Status (1)

Country Link
CN (1) CN207062259U (en)

Similar Documents

Publication Publication Date Title
CN206881716U (en) Chemical reaction kettle
CN207062259U (en) A kind of novel saccharification tank
CN204939500U (en) saccharifying tank
CN113181868A (en) Solid-phase tackifying reaction kettle and method
CN211051477U (en) Environment-friendly heating device's reation kettle
CN210612903U (en) Novel ball-type concentrator is used in medicine subsides production
CN207483754U (en) Outer circulation type multiple spot thermal compensation large size full-mixing type marsh gas anaerobic fermentation tank
CN211689086U (en) Protein polypeptide feed fermentation device
CN206285856U (en) A kind of material-compound tank water circulation system
CN209654762U (en) A kind of heat-insulation conveying device of chlorated liquid
CN208711721U (en) Highly effective reaction kettle
CN208182862U (en) A kind of high efficiency takes off plating tank
CN207101925U (en) A kind of energy-saving evaporator being concentrated by evaporation for glucose syrup
CN207002750U (en) One kind energy-conservation saccharifying tank
CN219217809U (en) Thermal hydrolysis reactor
CN105920869B (en) A kind of cooling fins, a kind of cooling fins formula crystallizing tank and its cooling means
CN209222094U (en) Suitable for the energy-efficient reaction kettle of feed additive production
CN220852618U (en) Urea rectifying column heat transfer device
CN210332669U (en) Polymerization reaction kettle
CN205570185U (en) Cold -storage agent manufacturing installation
CN205933833U (en) Automatic fermenting installation of controlled reaction process
CN217663367U (en) Tetrafluorobenzyl alcohol automatic reduction reaction equipment
CN221197392U (en) Energy-saving device for steam boiler
CN110586007A (en) Environment-friendly heating device's reation kettle
CN217411770U (en) High-efficiency cleaning device based on high-temperature turbulent water

Legal Events

Date Code Title Description
GR01 Patent grant
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: 20180302

Termination date: 20180801