CN209501028U - A kind of Preserved produciton liquid glucose cleaning treatment system - Google Patents

A kind of Preserved produciton liquid glucose cleaning treatment system Download PDF

Info

Publication number
CN209501028U
CN209501028U CN201822161998.XU CN201822161998U CN209501028U CN 209501028 U CN209501028 U CN 209501028U CN 201822161998 U CN201822161998 U CN 201822161998U CN 209501028 U CN209501028 U CN 209501028U
Authority
CN
China
Prior art keywords
liquid glucose
filter
liquid
preserved
connect
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
CN201822161998.XU
Other languages
Chinese (zh)
Inventor
李华东
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.)
Chengde Hua Long Food Co Ltd
Original Assignee
Chengde Hua Long Food 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 Chengde Hua Long Food Co Ltd filed Critical Chengde Hua Long Food Co Ltd
Priority to CN201822161998.XU priority Critical patent/CN209501028U/en
Application granted granted Critical
Publication of CN209501028U publication Critical patent/CN209501028U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Preparation Of Fruits And Vegetables (AREA)

Abstract

The utility model discloses a kind of Preserved produciton liquid glucose cleaning treatment systems, system is connect with Preserved produciton line, for receiving used liquid glucose in Preserved produciton line, including coarse filter, heating device, multistage enzymatic vessel, decolorization filtering unit, change sugared device, surge tank, sterilizing unit and finished pot, coarse filter is connect with the outlet for discharging liquid glucose on preserved fruit production line, heating device heats the filtered solution of coarse filter, it is delivered in multistage enzymatic vessel, multistage enzymatic vessel is to the pectin in solution, pomace enzymolysis processing, it decolourizes again through decolorization filtering unit, liquid glucose clear liquid is obtained after filtering, and it will be in the sugared device of being pumped into of liquid glucose clear liquid, it is pumped into finished pot after sterilizing unit is to the liquid glucose sterilization treatment changed in sugared device again, finished pot is connect with the Preserved produciton line.The utility model comes back to it in preserved fruit production line after handling the liquid glucose recycled, so as to avoid the waste of liquid glucose.

Description

A kind of Preserved produciton liquid glucose cleaning treatment system
Technical field
A kind of the utility model Preserved produciton technical field, and in particular to Preserved produciton liquid glucose cleaning treatment system.
Background technique
Preserved fruit is one of traditional properties food, its Yu Man capital, and be renown far and wide the whole nation, is sold abroad.China makes candied fruit Existing more than 1000 years history is so far by the most famous with Pekinese.Wherein the fruit such as mango, tomato, cumquat, apple are fruit Main material in Preserved produciton, syrup needs are used for multiple times, and the syrup after recycling, viscosity can increase, and color is deepened, Even become auburn sticky, muddy liquid glucose in the later period, such liquid glucose cannot enter back into the processing technology of preserved fruit, no Image can then be caused to liquid glucose quality, while can also be unfavorable for the health of eater, if direct emission can generate it is huge Waste, recycle the liquid glucose of multiple Reusability really, and health come back on Preserved produciton line, be mesh The technical issues of preceding urgent need to resolve, avoids Reusability from not handling liquid glucose, finally to generated used sugar The unhealthy processing mode that liquid is disposably discharged.It also avoids only simply filtering decolorization mode simultaneously, it is not right Harmful substance is handled in used liquid glucose, will also result in the unhealthy problem of finished fruit preserved after processing.
Utility model content
For the sugar solution of preserved fruit repeatedly used in the Preserved produciton in the presence of the prior art without professional skill Art processing the technical issues of being discharged or recycled, influencing preserved fruit product quality, the utility model provide a kind of preserved fruit and add Work liquid glucose cleaning treatment system.
A kind of Preserved produciton liquid glucose cleaning treatment system, the system are connect with Preserved produciton line, are added for receiving preserved fruit Used liquid glucose in work line successively includes coarse filter, heating device, multistage enzymatic vessel, decolorization filtering unit, changes sugar dress It sets, surge tank, sterilizing unit and finished pot, the coarse filter had been used by discharging on pipeline and the preserved fruit production line Liquid glucose outlet connection, for filtering out the impurity in used liquid glucose;The heating device is to the coarse filter Filtered solution is heated, and is delivered in the multistage enzymatic vessel, the multistage enzymatic vessel in solution pectin, Pomace carries out enzymolysis processing, then liquid glucose clear liquid is obtained after the decolorization filtering unit is decolourized, filtered, and by liquid glucose clear liquid It is pumped into the sugared device of describedization, then is pumped into after the sterilizing unit carries out sterilization treatment to the liquid glucose in the sugared device of describedization To in the finished pot, the finished pot is connect with the Preserved produciton line.
Preferably, the heating device is plate heat exchanger.
The decolorization filtering unit includes automatic discharge filter, cloth envelop collector and cardboard filter device, the automatic row Slag filter is connect with the multistage enzymatic vessel, and the cardboard filter device is connect with the sugared device of describedization, the solution warp after enzymatic hydrolysis Liquid glucose clear liquid is formed after the automatic discharge filter decoloration, gained liquid glucose clear liquid successively passes through the cloth envelop collector and cardboard Filter is filtered.
The automatic discharge filter includes shell and multiple rows of arc-shaped filter plate for being set in parallel positioned at enclosure interior With the activated carbon adsorption net for being attached at the arc-shaped filter plate lateral surface, the enclosure interior liquid glucose is through the activated carbon adsorption Net obtains liquid glucose clear liquid after adsorbing to the pigment in used liquid glucose, and liquid glucose clear liquid is drained into the Bag filter Device further filters.
Se Zhi≤85%, Tou Guang Shuai≤85% of liquid glucose clear liquid is obtained after the automatic discharge filter is decolourized.
Describedization sugar device includes changing sugar bowl, and the cardboard filter device is connected by pipeline and the feed inlet of describedization sugar bowl It connects, describedization sugar bowl is connect by pumping installations with the sterilizing unit.
When liquid glucose treated pol is not achieved some single-item soaks sugared pol require when, need on the liquid glucose basis handled well On add new white granulated sugar, for this purpose, the utility model, which is also provided in changing sugared device, changes sugared slot, the cardboard filter device passes through Pipeline is connect with the feed inlet of the sugared slot of describedization and change sugar bowl, and describedization sugar slot is connected by vaporising device and the sterilizing unit It connects.
Technical solutions of the utility model have the advantages that
A. the utility model is by carrying out coarse filtration for used liquid glucose used on Preserved produciton line, enzymatic hydrolysis, taking off Chromogenic filter changes sugar and sterilization processing, by used liquid glucose pectin and the impurity such as pomace digest, after enzymatic hydrolysis Used liquid glucose obtains clear liquid after decolorization filtering again, then again to the filtering of liquid glucose clear liquid further progress, change sugar and sterilization Processing forms finished product liquid glucose, if the various substances in detection liquid glucose can reach the standard of new sugar making liquid, can come back to preserved fruit In production line, so as to avoid the waste of liquid glucose, meanwhile, liquid glucose after processing will not cause any unfavorable shadow to the health of people It rings.
B. the utility model heats used liquid glucose before decolorization filtering, reaches enzymatic hydrolysis Optimum temperature, the solution after enzymatic hydrolysis is successively through automatic discharge filter, cloth envelop collector and cardboard filter device, through automatic discharge Filter carry out liquid glucose decolorization, complete liquid glucose clear liquid production, then successively through cloth envelop collector carry out coarse filtration and After cardboard filter device carries out the filtering of depth essence, so that solution is reached liquid glucose using standard, most changed sugar afterwards and sterilization is completed to liquid glucose The purified treatment of clear liquid, it is high-efficient.
C. existing liquid glucose is a bit darkish in color after utilizing several times and pol is insufficient, can assemble a large amount of ion, pigment etc., Not handling directly to cancel, by processing system provided by the utility model it is ensured that the recycling of liquid glucose, avoids making At a large amount of wastes.
Detailed description of the invention
In order to illustrate more clearly of specific embodiment of the present invention, will make below to required in specific embodiment Attached drawing is briefly described, it should be apparent that, the accompanying drawings in the following description is some embodiments of the utility model, right For those of ordinary skill in the art, without creative efforts, it can also be obtained according to these attached drawings His attached drawing.
Fig. 1 is a kind of Preserved produciton liquid glucose cleaning treatment system figure provided by the utility model;
Fig. 2 is automatic discharge filtering machine structure schematic diagram shown in Fig. 1.
Description of symbols:
1- coarse filter;2- heating device;3- multistage enzymatic vessel
4- decolorization filtering unit
41- automatic discharge filter
411- shell, 412- arc-shaped filter plate, 413- activated carbon adsorption net
42- cloth envelop collector, 43- cardboard filter device
5-ization sugar device
51-ization sugar bowl, 52-ization sugar slot
6- surge tank;7- sterilizing unit;8- finished pot;9- vaporising device.
Specific embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally Field those of ordinary skill every other embodiment obtained without making creative work belongs to practical Novel protected range.
As depicted in figs. 1 and 2, the utility model provides a kind of Preserved produciton liquid glucose cleaning treatment system, with preserved fruit Processing line connection successively includes coarse filter 1, heating device 2, more for receiving used liquid glucose in Preserved produciton line Grade enzymatic vessel 3, decolorization filtering unit 4, the sugared device 5 of change, surge tank 6, sterilizing unit 7 and finished pot 8, coarse filter 1 pass through pipe Road is connect with the outlet for discharging liquid glucose on preserved fruit production line, for filtering out the impurity in used liquid glucose;Heating device 2 The filtered solution of coarse filter 1 is heated, and is delivered in multistage enzymatic vessel 3, multistage enzymatic vessel 3 is to the fruit in solution Glue, pomace carry out enzymolysis processing, then clear liquid are obtained after decolorization filtering unit 4 is decolourized, filtered, and by being pumped into of clear liquid In sugared device 5, then the liquid glucose changed in sugared devices 5 through 7 Duis of sterilizing unit carry out sterilization treatment after be pumped into finished pot 8, finished product Tank 8 is connect with Preserved produciton line, and the liquid glucose in finished pot 8 is pumped into Preserved produciton line after adjusting.Here liquid glucose can be next From the used liquid glucose in processing workshop, it can also be the used liquid glucose outside workshop, carried out through this system After the enzymatic hydrolysis of liquid glucose, decoloration and filtering, the re-using to liquid glucose is realized, direct emission dirt caused by environment is avoided Dye, and the adverse effect that direct Reusability finds out quality of finished.
Heating device 2 employed in the utility model is preferably plate heat exchanger, is exchanged heat by steam to liquid glucose, So that the temperature of used liquid glucose is reached best hydrolysis temperature, is conducive to improve the substances such as pectin, pomace, pericarp in liquid glucose Enzymolysis efficiency.
The decolorization filtering unit 4 employed in entire recovery and processing system includes automatic discharge filter 41, cloth bag mistake Filter 42 and cardboard filter device 43, automatic discharge filter 41 are connect with multistage enzymatic vessel 3, cardboard filter device 43 and the sugared device of change 5 connect, and the solution after enzymatic hydrolysis forms clear liquid after the decoloration of automatic discharge filter 41, and gained liquid glucose clear liquid is successively through Bag filter Device 42 and cardboard filter device 43 are filtered.Liquid glucose clear liquid after 42 pairs of cloth envelop collector decolorations therein plays coarse filtration work With, then through cardboard filter device 4 to the further essence filtering of liquid glucose clear liquid.It is clear that liquid glucose is obtained after automatic discharge filter is decolourized Se Zhi≤85%, Tou Guang Shuai≤85% of liquid.
As shown in Fig. 2, automatic discharge filter 41 used by the utility model is including shell 411 and is located at shell 411 The arc-shaped filter plate 412 and activated carbon adsorption net 413 of internal multiple rows of parallel interval setting, arc-shaped filter plate 411 are located at The medial surface of activated carbon adsorption net 413, arc-shaped filter plate 411 play support fixed function to activated carbon adsorption net 413, are located at Liquid in arc-shaped filter plate 412 adsorbs the pigment in filtered fluid through activated carbon adsorption net 413, obtains liquid glucose Clear liquid, and liquid glucose clear liquid is drained into the further coarse filtration of cloth envelop collector 42.
In conjunction with Fig. 2, the working principle of automatic discharge filter is as follows: the liquid glucose after enzymatic hydrolysis is entered in shell and filled through pump Full, under the effect of the pressure, the solid impurity in liquid glucose is tightly held by activated carbon net retention, and forms filter on the net in activated carbon adsorption Cake, liquid glucose enters outlet tube outflow shell through filter tip through activated carbon adsorption net, to obtain clear liquid glucose.
With the increase of filtration time, it is more and more to be trapped within the online solid impurity of activated carbon adsorption, keeps filter cake thick Degree is continuously increased, and filtration resistance increases, and the intracorporal pressure rise of shell needs deslagging when pressure is raised to certain value, stops to shell Input in vivo then passes to steam drying filter cake to liquid glucose.Steam off opens butterfly valve, starts vibrator, filters arc-shaped Panel vibration falls the online filter cake vibration of activated carbon adsorption through slag-drip opening discharge below shell.The utility model is filtered in arc-shaped Activated carbon adsorption net is laid with and fixed on plate, that is, realizes the retention to filter residue, while also achieving to all colours in liquid glucose It is adsorbed, realizes the fast purification of color in liquid glucose, it is high-efficient, meet production requirement.
Thereinization sugar device 5 includes changing sugar bowl 51, and cardboard filter device 43 is connected by pipeline with the feed inlet for changing sugar bowl 51 It connects, changes sugar bowl 51 and connect by pumping installations with sterilizing unit 7.
When liquid glucose treated pol is not achieved some single-item soaks sugared pol require when, need on the liquid glucose basis handled well On add new white granulated sugar, for this purpose, the utility model, which is also provided in changing sugared device, changes sugared slot, cardboard filter device passes through pipeline It is connect with the feed inlet for changing sugared slot and change sugar bowl, changes sugared slot and connect by vaporising device with sterilizing unit.
Change liquid glucose in sugared slot to enter in surge tank 6 after two vaporising devices, then carries out last go out through sterilizing unit 7 Bacterium processing, makes the liquid glucose separated from liquid glucose reach sanitary index, comes back on Preserved produciton production line and utilize, will not be right The mouthfeel of preserved fruit product quality has any impact, and substantially increases the utilization rate to resource.
Obviously, the above embodiments are merely examples for clarifying the description, and does not limit the embodiments.It is right For those of ordinary skill in the art, can also make on the basis of the above description it is other it is various forms of variation or It changes.There is no necessity and possibility to exhaust all the enbodiments.And it is extended from this it is obvious variation or It changes among still in the protection scope of the utility model.

Claims (7)

1. a kind of Preserved produciton liquid glucose cleaning treatment system, which is characterized in that the system is connect with Preserved produciton line, for connecing Used liquid glucose in Preserved produciton line is received, successively includes coarse filter (1), heating device (2), multistage enzymatic vessel (3), take off Chromogenic filter unit (4) changes sugared device (5), surge tank (6), sterilizing unit (7) and finished pot (8), and the coarse filter (1) is logical It crosses pipeline and is connect with the outlet for discharging liquid glucose on the Preserved produciton line, for filtering out the impurity in used liquid glucose; The heating device (2) heats the coarse filter (1) filtered solution, and is delivered to the multistage enzymatic vessel (3) in, the multistage enzymatic vessel (3) carries out enzymolysis processing to the pectin in solution, pomace, then through the decolorization filtering unit (4) liquid glucose clear liquid is obtained after being decolourized, being filtered, and liquid glucose clear liquid is pumped into describedization sugar device (5), then is killed described in passing through Bacterium device (7) is pumped into the finished pot (8) after carrying out sterilization treatment to the liquid glucose in the sugared device of describedization (5), it is described at Product tank (8) is connect with the Preserved produciton line.
2. a kind of Preserved produciton liquid glucose cleaning treatment system according to claim 1, which is characterized in that the heating device It (2) is plate heat exchanger.
3. a kind of Preserved produciton liquid glucose cleaning treatment system according to claim 1, which is characterized in that the decolorization filtering Unit (4) includes automatic discharge filter (41), cloth envelop collector (42) and cardboard filter device (43), the automatic discharge filtering Machine (41) is connect with the multistage enzymatic vessel (3), and the cardboard filter device (43) connect with the sugared device (5) of describedization, after enzymatic hydrolysis Solution form liquid glucose clear liquid after the automatic discharge filter (41) decoloration, gained liquid glucose clear liquid successively passes through the cloth bag Filter (42) and cardboard filter device (43) are filtered.
4. a kind of Preserved produciton liquid glucose cleaning treatment system according to claim 3, which is characterized in that the automatic discharge Filter (41) include shell (411) and be located inside shell (411) multiple rows of arc-shaped filter plate (412) for being set in parallel and It is attached at the activated carbon adsorption net (413) of arc-shaped filter plate (412) lateral surface, the internal liquid glucose warp of the shell (411) The activated carbon adsorption net (413) obtains liquid glucose clear liquid after adsorbing to the pigment in liquid glucose, and liquid glucose clear liquid is drained into institute Cloth envelop collector (42) is stated further to filter.
5. a kind of Preserved produciton liquid glucose cleaning treatment system according to claim 4, which is characterized in that through the automatic row Slag filter obtains Se Zhi≤85%, Tou Guang Shuai≤85% of liquid glucose clear liquid after being decolourized.
6. according to a kind of Preserved produciton liquid glucose cleaning treatment system as claimed in claim 3 to 5, which is characterized in that describedization Sugared device (5) includes changing sugar bowl (51), and the cardboard filter device (43) is connected by pipeline and the feed inlet of describedization sugar bowl (51) It connects, describedization sugar bowl (51) is connect by pumping installations with the sterilizing unit (7).
7. a kind of Preserved produciton liquid glucose cleaning treatment system according to claim 6, which is characterized in that describedization sugar device (5) the sugared slot of further including (52), the cardboard filter device (43) is by pipeline and the sugared slot (52) of describedization and changes sugar bowl (51) Feed inlet connection, describedization sugar slot (52) are connect by vaporising device (9) with the sterilizing unit (7).
CN201822161998.XU 2018-12-23 2018-12-23 A kind of Preserved produciton liquid glucose cleaning treatment system Active CN209501028U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201822161998.XU CN209501028U (en) 2018-12-23 2018-12-23 A kind of Preserved produciton liquid glucose cleaning treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201822161998.XU CN209501028U (en) 2018-12-23 2018-12-23 A kind of Preserved produciton liquid glucose cleaning treatment system

Publications (1)

Publication Number Publication Date
CN209501028U true CN209501028U (en) 2019-10-18

Family

ID=68196385

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201822161998.XU Active CN209501028U (en) 2018-12-23 2018-12-23 A kind of Preserved produciton liquid glucose cleaning treatment system

Country Status (1)

Country Link
CN (1) CN209501028U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109647047A (en) * 2018-12-23 2019-04-19 承德华朗食品有限公司 A kind of Preserved produciton liquid glucose cleaning treatment system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109647047A (en) * 2018-12-23 2019-04-19 承德华朗食品有限公司 A kind of Preserved produciton liquid glucose cleaning treatment system
CN109647047B (en) * 2018-12-23 2024-05-24 承德华朗食品有限公司 Preserved fruit processing sugar liquid purifying treatment system

Similar Documents

Publication Publication Date Title
CN206924486U (en) Oil filtration system
CN105087833B (en) A kind of process for industrializing zero addition brown sugar of continous way production
CN209501028U (en) A kind of Preserved produciton liquid glucose cleaning treatment system
CN206915905U (en) A kind of environment protection type paper wastewater treatment equipment
CN109647047A (en) A kind of Preserved produciton liquid glucose cleaning treatment system
CN103520979A (en) Special vacuum-type drum filter for treating ultrafiltration tank bottom substances and treatment method of ultrafiltration tank bottom substances
CN111575413A (en) Brown sugar processing device and process
CN210993018U (en) Microwave drying device for producing instant agar
CN204502441U (en) A kind of Medical liquor extraction apparatus
CN105732739A (en) Technique for extracting and purifying stevioside from stevia
CN206955830U (en) A kind of hydraulic engineering apparatus for treating sewage
CN210583908U (en) A filter equipment for producing barium chloride
CN108514811A (en) In a kind of yellow phosphoric tail gas boiler acid liquor filtering and device
CN105148557B (en) A kind of syrup decolorization system
CN107952273A (en) A kind of carclazyte filtration apparatus
CN103012602B (en) Purified starch eddy flow washing system
CN209113835U (en) A kind of peony seed oil production line
CN113331376A (en) Pickled Chinese cabbage fermentation desalting system and method
CN104862428B (en) The sugar-free grains enrichment and separation device and method of a kind of enzyme process starch sugar
CN207042053U (en) A kind of strong brine zero discharge treatment device
CN207429839U (en) A kind of ferment clarification filtration equipment
CN205874343U (en) Membrane type filtration section of thick bamboo that olive oil production line was used
CN206978704U (en) A kind of fig processes pretreating device
CN206008224U (en) A kind of membrane type filter core for olive oil production line
CN110684596A (en) Tea oil purification method

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant