CN207101918U - A kind of evaporator being concentrated by evaporation for glucose syrup - Google Patents

A kind of evaporator being concentrated by evaporation for glucose syrup Download PDF

Info

Publication number
CN207101918U
CN207101918U CN201720925600.8U CN201720925600U CN207101918U CN 207101918 U CN207101918 U CN 207101918U CN 201720925600 U CN201720925600 U CN 201720925600U CN 207101918 U CN207101918 U CN 207101918U
Authority
CN
China
Prior art keywords
evaporation
steam
glucose syrup
concentrated
housing
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
CN201720925600.8U
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 CN201720925600.8U priority Critical patent/CN207101918U/en
Application granted granted Critical
Publication of CN207101918U publication Critical patent/CN207101918U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Confectionery (AREA)

Abstract

It the utility model is related to glucose syrup production equipment field, more particularly to a kind of evaporator being concentrated by evaporation for glucose syrup.Including housing, the housing is provided with steam inlet duct, steam outleting pipe, and the enclosure interior is provided with steam pipe coil, and the steam pipe coil connects the steam inlet duct and the steam outleting pipe, electrically-controlled valve is provided with the steam inlet duct;The housing tip is provided with steam exhaust-gas mouth;The lower housing portion is provided with feed pipe, and the housing upper is provided with discharge nozzle;Syrup concentration detector and Electrocontrolled tee valve are installed on the discharge nozzle;3rd end of the Electrocontrolled tee valve connects the feed pipe by pipeline;The syrup concentration detector, the electrically-controlled valve, the Electrocontrolled tee valve electrically connect with central processing unit respectively.The purpose of this utility model is to provide a kind of evaporator being concentrated by evaporation for glucose syrup, to solve the problems, such as that the evaporator automatization level for being currently used for glucose syrup evaporation and concentration is low.

Description

A kind of evaporator being concentrated by evaporation for glucose syrup
Technical field
Glucose syrup production equipment field is the utility model is related to, it is more particularly to a kind of to be used for what glucose syrup was concentrated by evaporation Evaporator.
Background technology
, it is necessary to be evaporated concentration to the syrup after decolorization filtering in glucose syrup production process, by glucose syrup Water evaporation, improve glucose syrup concentration, now need to use evaporator, the existing evaporation being concentrated by evaporation for glucose syrup Device automatization level is low, manually judges grape concentration of slurry, and judging nicety rate is low, easily causes glucose syrup concentration and does not conform to Lattice, concentration it is too low or it is too high be required for handling again, increase workload, cause the wasting of resources.
Utility model content
The purpose of this utility model is to provide a kind of evaporator being concentrated by evaporation for glucose syrup, to solve existing use In glucose syrup be concentrated by evaporation evaporator automatization level it is low the problem of.
The purpose of this utility model is realized by following technical proposals:
A kind of evaporator being concentrated by evaporation for glucose syrup, it includes housing, the housing provided with steam inlet duct, Steam outleting pipe, the enclosure interior are provided with steam pipe coil, and the steam pipe coil connects the steam inlet duct and the steam Escape pipe, electrically-controlled valve is installed on the steam inlet duct;The housing tip is provided with steam exhaust-gas mouth;The lower housing portion is set There is feed pipe, the housing upper is provided with discharge nozzle;Syrup concentration detector and Electrocontrolled tee valve are installed on the discharge nozzle; 3rd end of the Electrocontrolled tee valve connects the feed pipe by pipeline;The syrup concentration detector, the electrically-controlled valve, institute Electrocontrolled tee valve is stated to electrically connect with central processing unit respectively.
Further, dividing plate is provided with the housing, the dividing plate top is the first cavity, and described the lower partition is second Cavity;The dividing plate is provided with spout hole;The steam pipe coil is arranged in first cavity;It is provided with second cavity Heat exchange coil;The heat exchange coil both ends connect injection liquefaction feed mouth and injection liquefaction discharging opening respectively.
Further, deflector is provided with second cavity, the deflector installation is on the housing.
Further, the deflector has two or more, and each deflector is disposed on the both sides of the housing.
Further, in addition to motor and agitating device;The agitating device connects the motor;The agitating device is set It is placed in first cavity.
Further, the steam pipe coil is made up of aluminum alloy materials.
Further, the syrup concentration detector is MHY-18987 series syrup concentration detectors.
Further, the Electrocontrolled tee valve is ZN/L-DV3000 series Electrocontrolled tee valves.
Further, the electrically-controlled valve is JL900 series electrical ball valves.
Further, the central processing unit is IST200 central series processors.
The utility model has the following advantages that compared with prior art:
1. the evaporator described in the utility model being concentrated by evaporation for glucose syrup, it includes housing, set on the housing There are steam inlet duct, steam outleting pipe, the enclosure interior is provided with steam pipe coil, and the steam pipe coil connects the steam inlet Pipe and the steam outleting pipe, electrically-controlled valve is installed on the steam inlet duct;The housing tip is provided with steam exhaust-gas mouth;Institute State lower housing portion and be provided with feed pipe, the housing upper is provided with discharge nozzle;Syrup concentration detector is installed on the discharge nozzle And Electrocontrolled tee valve;3rd end of the Electrocontrolled tee valve connects the feed pipe by pipeline;The syrup concentration detector, The electrically-controlled valve, the Electrocontrolled tee valve electrically connect with central processing unit respectively;Syrup concentration detector monitors discharge nozzle in real time The concentration of middle glucose syrup, monitoring signals are passed into central processing unit, if glucose syrup concentration meets the requirements, central processing Device transmits signal and discharges glucose syrup to Electrocontrolled tee valve, Electrocontrolled tee valve action, connection discharge nozzle;If glucose syrup is dense Spend undesirable, central processing unit transmission signal to Electrocontrolled tee valve, Electrocontrolled tee valve action, connection feed pipe and discharging Pipe, makes glucose syrup reenter in housing, while central processing unit transmits signal to electrically-controlled valve, changes the aperture of electrically-controlled valve, Adjust vapor (steam) temperature in steam pipe coil;This structure can realize the automatic of glucose syrup concentration during glucose syrup concentration and evaporation Regulation.
2. being provided with dividing plate in the utility model housing, the dividing plate top is the first cavity, and described the lower partition is second Cavity;The dividing plate is provided with spout hole;The steam pipe coil is arranged in first cavity;It is provided with second cavity Heat exchange coil;The heat exchange coil both ends connect injection liquefaction feed mouth and injection liquefaction discharging opening respectively;Glucose syrup produces During, it is necessary to carry out injection liquefaction, spray that liquefied slurry temperature is higher, this structure can utilize the slurries after injection liquefaction Grape slurries are heated, improve energy utilization rate.
3. being provided with deflector in the second cavity described in the utility model, the deflector installation is on the housing;It is described Deflector has two or more, and each deflector is disposed on the both sides of the housing;Grape slurry liquid can be made in the second chamber Internal S types flowing, increases grape slurry fluidity, improves heat transfer effect.
Brief description of the drawings
Fig. 1 is the evaporation structure figure described in the utility model being concentrated by evaporation for glucose syrup;
Fig. 2 is the utility model electrical connection diagram;
In figure:1- electrically-controlled valves, 2- steam inlet ducts, 3- steam exhaust-gas mouth, 4- housings, 5- discharge nozzles, the inspection of 6- syrup concentrations Instrument, 7- Electrocontrolled tee valves, 8- steam pipe coils, the cavitys of 9- first, 10- steam outleting pipes, 11- injection liquefaction feeds mouth, 12- is surveyed to change Hot coil, 13- deflectors, 14- injection liquefaction discharging opening, the cavitys of 15- second, 16- feed pipes, 17- motors, 18- agitating devices, 19- dividing plates, 20- spout holes.
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, Fig. 2, a kind of evaporator being concentrated by evaporation for glucose syrup, it includes housing 4, and housing 4 is provided with Steam inlet duct 2, steam outleting pipe 10, the inside of housing 4 are provided with steam pipe coil 8, and steam pipe coil 8 connects steam inlet duct 2 and steamed Vapour escape pipe 10, electrically-controlled valve 1 is installed on steam inlet duct 2;The top of housing 4 is provided with steam exhaust-gas mouth 3;The bottom of housing 4 is provided with Feed pipe 16, the top of housing 4 are provided with discharge nozzle 5;Syrup concentration detector 6 and Electrocontrolled tee valve 7 are installed on discharge nozzle 5;Electricity The 3rd end for controlling triple valve 7 connects feed pipe 16 by pipeline;Syrup concentration detector 6, electrically-controlled valve 1, Electrocontrolled tee valve 7 divide Do not electrically connected with central processing unit;Syrup concentration detector 6 monitors the concentration of glucose syrup in discharge nozzle 5 in real time, and monitoring is believed Number central processing unit is passed to, if glucose syrup concentration meets the requirements, central processing unit transmits signal to Electrocontrolled tee valve 7, Electrocontrolled tee valve 7 acts, and connection discharge nozzle 5 discharges glucose syrup;If glucose syrup concentration is undesirable, central processing Device transmits signal and acted to Electrocontrolled tee valve 7, Electrocontrolled tee valve 7, connects feed pipe 16 and discharge nozzle 5, makes glucose syrup again Into in housing 4, while central processing unit transmits signal to electrically-controlled valve 1, changes the aperture of electrically-controlled valve 1, adjusts in steam pipe coil 8 Vapor (steam) temperature;This structure can realize automatically adjusting for glucose syrup concentration during glucose syrup concentration and evaporation;Syrup concentration Detector 6 is MHY-18987 series syrup concentration detectors;Electrocontrolled tee valve 7 is ZN/L-DV3000 series Electrocontrolled tee valves; Electrically-controlled valve 1 is JL900 series electrical ball valves;The central processing unit is IST200 central series processors.
Referring to Fig. 1, dividing plate 19 is provided with housing 4, the top of dividing plate 19 is the first cavity 9, and the bottom of dividing plate 19 is the second cavity 15;Dividing plate 19 is provided with spout hole 20;Steam pipe coil 8 is arranged in the first cavity 9;Heat exchange coil is provided with second cavity 15 12;The both ends of heat exchange coil 12 connect injection liquefaction feed mouth 11 and injection liquefaction discharging opening 14 respectively;Glucose syrup production process In, it is necessary to carry out injection liquefaction, it is higher to spray liquefied slurry temperature, reaches 100 degree or so, and the Portugal before being concentrated by evaporation Grape syrup temp is 50 degree or so, and this structure can utilize the slurries after injection liquefaction to heat grape slurries, improve the energy Utilization rate.
Referring to Fig. 1, deflector 13 is provided with the second cavity 15, deflector 13 is arranged on housing 4;Deflector 13 has two More than, each deflector 13 is disposed on the both sides of housing 4;It can flow grape slurry liquid S types in the second cavity 15, increase Grape slurry fluidity, improve heat transfer effect.
Referring to Fig. 1, the utility model also includes motor 17 and agitating device 18;Agitating device 18 connects motor 17;Stirring Device 18 is arranged in the first cavity 9;Agitating device 18 is stirred to glucose syrup, strengthens the mobility of glucose syrup, is increased Big glucose syrup contacts with steam pipe coil 8, improves heat exchange efficiency, and promote the exclusion of steam in glucose syrup.
Referring to Fig. 1, steam pipe coil 8 is made up of aluminum alloy materials, and aluminum alloy materials density is low, and intensity is higher, has good Heat conductivility.
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. evaporator being concentrated by evaporation for glucose syrup, it is characterised in that:Including housing, the housing is provided with steam Air inlet pipe, steam outleting pipe, the enclosure interior are provided with steam pipe coil, and the steam pipe coil connects the steam inlet duct and institute Steam outleting pipe is stated, electrically-controlled valve is installed on the steam inlet duct;The housing tip is provided with steam exhaust-gas mouth;The housing Bottom is provided with feed pipe, and the housing upper is provided with discharge nozzle;Syrup concentration detector and automatically controlled is installed on the discharge nozzle Triple valve;3rd end of the Electrocontrolled tee valve connects the feed pipe by pipeline;The syrup concentration detector, the electricity Control valve, the Electrocontrolled tee valve electrically connect with central processing unit respectively.
  2. 2. the evaporator according to claim 1 being concentrated by evaporation for glucose syrup, it is characterised in that:Set in the housing There is dividing plate, the dividing plate top is the first cavity, and described the lower partition is the second cavity;The dividing plate is provided with spout hole;Institute Steam pipe coil is stated to be arranged in first cavity;Heat exchange coil is provided with second cavity;The heat exchange coil both ends point Liquefaction feed mouth and injection liquefaction discharging opening Lian Jie not sprayed.
  3. 3. the evaporator according to claim 2 being concentrated by evaporation for glucose syrup, it is characterised in that:Second cavity Interior to be provided with deflector, the deflector installation is on the housing.
  4. 4. the evaporator according to claim 3 being concentrated by evaporation for glucose syrup, it is characterised in that:The deflector has Two or more, each deflector are disposed on the both sides of the housing.
  5. 5. the evaporator according to claim 2 being concentrated by evaporation for glucose syrup, it is characterised in that:Also include motor and Agitating device;The agitating device connects the motor;The agitating device is arranged in first cavity.
  6. 6. the evaporator according to claim 1 being concentrated by evaporation for glucose syrup, it is characterised in that:The steam pipe coil It is made up of aluminum alloy materials.
  7. 7. the evaporator according to claim 1 being concentrated by evaporation for glucose syrup, it is characterised in that:The syrup concentration Detector is MHY-18987 series syrup concentration detectors.
  8. 8. the evaporator according to claim 1 being concentrated by evaporation for glucose syrup, it is characterised in that:The automatically controlled threeway Valve is ZN/L-DV3000 series Electrocontrolled tee valves.
  9. 9. the evaporator according to claim 1 being concentrated by evaporation for glucose syrup, it is characterised in that:The electrically-controlled valve is JL900 series electrical ball valves.
  10. 10. the evaporator according to claim 1 being concentrated by evaporation for glucose syrup, it is characterised in that:The centre Reason device is IST200 central series processors.
CN201720925600.8U 2017-07-27 2017-07-27 A kind of evaporator being concentrated by evaporation for glucose syrup Expired - Fee Related CN207101918U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720925600.8U CN207101918U (en) 2017-07-27 2017-07-27 A kind of evaporator being concentrated by evaporation for glucose syrup

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720925600.8U CN207101918U (en) 2017-07-27 2017-07-27 A kind of evaporator being concentrated by evaporation for glucose syrup

Publications (1)

Publication Number Publication Date
CN207101918U true CN207101918U (en) 2018-03-16

Family

ID=61579964

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720925600.8U Expired - Fee Related CN207101918U (en) 2017-07-27 2017-07-27 A kind of evaporator being concentrated by evaporation for glucose syrup

Country Status (1)

Country Link
CN (1) CN207101918U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113287776A (en) * 2021-07-07 2021-08-24 河南卷烟工业烟草薄片有限公司 Pulping concentration control system for paper-making reconstituted tobacco

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113287776A (en) * 2021-07-07 2021-08-24 河南卷烟工业烟草薄片有限公司 Pulping concentration control system for paper-making reconstituted tobacco

Similar Documents

Publication Publication Date Title
CN207101918U (en) A kind of evaporator being concentrated by evaporation for glucose syrup
CN206911337U (en) A kind of temperature can adjust reactor
CN207101925U (en) A kind of energy-saving evaporator being concentrated by evaporation for glucose syrup
CN207162689U (en) Pipe network balance-conditioning system of heat supply and heating network
CN207147036U (en) Cooling aerial cooler with humidification function
CN204987466U (en) Circular heat pump air can water heater
CN204478900U (en) A kind of efficient condenser
CN206399230U (en) A kind of Rapid Circulation device
CN206399045U (en) Evaporation coil and evaporator
CN209752879U (en) Molecular sieve reaction kettle rapid cooling process device
CN206772074U (en) Circulating water Tower System
CN206027141U (en) Be used for refine crystallization device of chlorophenol
CN205307857U (en) Vertical forced circulation vacuum hot crystallizer
CN218596483U (en) Vacuum coating machine cavity cooling device
CN207688324U (en) A kind of air-conditioning refrigeration plant accelerating refrigeration
CN218901803U (en) Cooling device for reaction kettle
CN104266297A (en) Water air conditioning evaporator and air conditioning plant
CN217361666U (en) Spray bubbling humidifier for fuel cell testing equipment
CN210728735U (en) A simple and easy evaporation crystallization device for copper sulfate production
CN213090521U (en) Water temperature control system
CN209623404U (en) Chilling tower cooler device
CN215413268U (en) Sulfonation reaction waste heat utilization equipment and sulfonation reaction device
CN216935958U (en) Energy-efficient reation kettle heating and refrigeration temperature control system
CN214469555U (en) Circulating water cooling system for circulating water vacuum pump
CN114486706B (en) Combined saturated humidifying barrel

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180316

Termination date: 20180727

CF01 Termination of patent right due to non-payment of annual fee