CN207562358U - A kind of syrup concentration pan - Google Patents

A kind of syrup concentration pan Download PDF

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Publication number
CN207562358U
CN207562358U CN201721230119.3U CN201721230119U CN207562358U CN 207562358 U CN207562358 U CN 207562358U CN 201721230119 U CN201721230119 U CN 201721230119U CN 207562358 U CN207562358 U CN 207562358U
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China
Prior art keywords
tank
concentration
heating cabinet
concentration tank
pumping
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Active
Application number
CN201721230119.3U
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Chinese (zh)
Inventor
薛冰
刘艳飞
路鸿霞
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 Da Shu Da Fu Special Food Co Ltd
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Shandong Da Shu Da Fu Special Food Co Ltd
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Priority to CN201721230119.3U priority Critical patent/CN207562358U/en
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Abstract

The utility model is related to production of condiments fields, particularly disclose a kind of syrup concentration pan.It includes offgas duct, storage tank and several groups of enrichment facilities, enrichment facility includes concentration tank and pumping tank, include feeding warehouse in concentration tank, heating cabinet and discharging bin, several tremie pipes are equipped in heating cabinet, tremie pipe connects feeding warehouse with discharging bin, discharging bin is connected with pumping tank, the heating cabinet of one of them concentration tank is connected with offgas duct, zigzag thbe connection is passed sequentially through between the heating cabinet of two neighboring concentration tank, the heating cabinet of the last one concentration tank and all pumping tanks connect respectively with drainer, storage tank is connected by dnockout pumps with the feeding warehouse of each concentration tank, the concentration tank of each group of enrichment facility reconnects mateiral pump after being connected with the lower end of pumping tank.The utility model carries out syrup heating by the tail gas that drying tower generates, and saves steam, has saved the energy, and the steam finally generated is recycled again, saved the energy again.

Description

A kind of syrup concentration pan
Technical field
The utility model is related to production of condiments field, more particularly to a kind of syrup concentration pan.
Background technology
In the production process of maltose, first have to starch that syrup is made, its concentration is relatively low after syrup is carried out, therefore will It is concentrated, concentration process is by steam heating evaporation, and steam usage amount is larger, but the tail due to being generated from drying tower steams Vapour carries a part of heat, and waste is bound to cause if directly exhausted.
Invention content
The defects of the utility model is in order to make up the prior art provides a kind of energy saving syrup concentration pan.
The utility model is achieved by the following technical solution:
A kind of syrup concentration pan, it is characterized in that, including offgas duct, storage tank and several groups of enrichment facilities, the concentration dress It puts including concentration tank and pumping tank, is followed successively by feeding warehouse, heating cabinet and discharging bin in the concentration tank from top to bottom, in heating cabinet Equipped with several tremie pipes, the tremie pipe connects feeding warehouse with discharging bin, and the discharging bin is connected with pumping tank, one of them The heating cabinet of the concentration tank is connected with offgas duct, zigzag thbe connection is passed sequentially through between the heating cabinet of two neighboring concentration tank, most The heating cabinet of the latter concentration tank and all pumping tanks connect respectively with drainer, and the storage tank passes through dnockout pumps and each The feeding warehouse connection of concentration tank, the concentration tank of each group of enrichment facility reconnect mateiral pump after being connected with the lower end for being evacuated tank.
Share four groups of enrichment facilities.
The beneficial effects of the utility model are:
The utility model carries out syrup heating by the tail gas that drying tower generates, and saves steam, has saved the energy, and The steam finally generated is recycled again, has saved the energy again.
Description of the drawings
The utility model will be further described below with reference to the accompanying drawings:
Fig. 1 is the connection of the utility model, broken section structure diagram.
In figure, 1 offgas duct, 2 concentration tanks, 21 feeding warehouses, 22 cavitys, 23 tremie pipes, 24 discharging bins, 3 pumping tanks, 4 storings Tank, 5 zigzag thbes, 6 dnockout pumps, 7 mateiral pumps, 8 drainers.
Specific embodiment
Attached drawing is specific embodiment of the utility model.As shown in Figure 1, this kind of syrup concentration pan, including offgas duct 1, storage Batch can 4 and four groups of enrichment facilities, four groups of enrichment facilities are from left to right in one line, and each group of enrichment facility includes 2 He of concentration tank Tank 3 is evacuated, feeding warehouse 21, heating cabinet and discharging bin 24 is followed successively by concentration tank 2 from top to bottom, several blankings is equipped in heating cabinet Pipe 23, tremie pipe 23 connect feeding warehouse 21 with discharging bin 24, are cavity 22 around tremie pipe 23, discharging bin 24 and pumping tank 3 Connection, the heating cabinet of the wherein concentration tank 2 of rightmost are connected with offgas duct 1, between the heating cabinet of two neighboring concentration tank 2 successively It is connected by zigzag thbe 5, the heating cabinet of leftmost concentration tank 2 and all pumping tanks 3 connect respectively with drainer 8, storage tank 4 Connected by dnockout pumps 7 with the feeding warehouse 21 of each concentration tank 2, can with 2 mating dnockout pumps 7 of each concentration tank, A dnockout pumps 7 can be shared with four concentration tanks 2, after the concentration tank 2 of each group of enrichment facility is connected with the lower end for being evacuated tank 3 Reconnect mateiral pump 7.
The course of work is as follows:Dnockout pumps 7 and offgas duct 1 are opened simultaneously, and syrup is entered each from storage tank 4 by dnockout pumps 7 In the feeding warehouse 21 of a concentration tank 2, enter discharging bin 24 from feeding warehouse 21 by tremie pipe 23, at the same time, offgas duct 1 comes out Tail gas enter the heating cabinet of rightmost the syrup in tremie pipe 23 heated, then enter next concentration from zigzag thbe 5 In the heating cabinet of tank 2, water is condensed into until entering in condenser pipe, syrup can carry some hot gas after entering discharging bin 24, these Hot gas, which is drawn into pumping tank 3 and then is passed through condenser pipe interior energy again, congeals into water, in the process if being pumped into part syrup, this portion Divide syrup that can be flowed out again by being evacuated the outlet of tank 3, into mateiral pump 7, and enter the syrup of discharging bin 24 also by pumping Material pump 7 is transported to next process.
In addition to technical characteristic described in specification, remaining technical characteristic is technology known to those skilled in the art.

Claims (2)

1. a kind of syrup concentration pan, it is characterized in that, including offgas duct(1), storage tank(4)It is described dense with several groups of enrichment facilities Compression apparatus includes concentration tank(2)With pumping tank(3), the concentration tank(2)It is inside followed successively by feeding warehouse from top to bottom(21), heating cabinet And discharging bin(24), heating cabinet is interior to be equipped with several tremie pipes(23), the tremie pipe(23)By feeding warehouse(21)And discharging bin (24)Connection, the discharging bin(24)With being evacuated tank(3)Connection, one of them described concentration tank(2)Heating cabinet and offgas duct (1)Connection, two neighboring concentration tank(2)Heating cabinet between pass sequentially through zigzag thbe(5)Connection, the last one concentration tank(2)'s Heating cabinet and all pumping tanks(3)Respectively with drainer(8)Connection, the storage tank(4)Pass through dnockout pumps(6)It is dense with each Contracting tank(2)Feeding warehouse(21)Connection, the concentration tank of each group of enrichment facility(2)With pumping tank(3)Lower end be connected after again Connect mateiral pump(7).
2. syrup concentration pan according to claim 1, it is characterized in that, share four groups of enrichment facilities.
CN201721230119.3U 2017-09-25 2017-09-25 A kind of syrup concentration pan Active CN207562358U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721230119.3U CN207562358U (en) 2017-09-25 2017-09-25 A kind of syrup concentration pan

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721230119.3U CN207562358U (en) 2017-09-25 2017-09-25 A kind of syrup concentration pan

Publications (1)

Publication Number Publication Date
CN207562358U true CN207562358U (en) 2018-07-03

Family

ID=62694595

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721230119.3U Active CN207562358U (en) 2017-09-25 2017-09-25 A kind of syrup concentration pan

Country Status (1)

Country Link
CN (1) CN207562358U (en)

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