CN203342963U - High-pressure rotational-flow reverse-rolling continuous separation device - Google Patents
High-pressure rotational-flow reverse-rolling continuous separation device Download PDFInfo
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- CN203342963U CN203342963U CN 201320348693 CN201320348693U CN203342963U CN 203342963 U CN203342963 U CN 203342963U CN 201320348693 CN201320348693 CN 201320348693 CN 201320348693 U CN201320348693 U CN 201320348693U CN 203342963 U CN203342963 U CN 203342963U
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Abstract
The utility model discloses a high-pressure rotational-flow reverse-rolling continuous separation device which comprises a machine frame platform, a power distribution cabinet, rolling continuous separation equipment and an alcohol metering container, wherein the power distribution cabinet, the rolling continuous separation equipment and the alcohol metering container are arranged on the machine frame platform; the rolling continuous separation equipment is electrically connected with the power distribution cabinet; the rolling continuous separation equipment comprises a feeding tank, rotational-flow separation devices, a waste liquid discharging pipe, a waste collecting pipe, a liquid discharging pipe and a collecting pipe; the feeding tank is provided with the liquid discharging pipe; and the rotational-flow separation devices are serially connected in sequence through the liquid discharging pipe and serially connected at an interval through the waste liquid discharging pipe. According to the high-pressure rotational-flow reverse-rolling continuous separation device, a structure that the multiple groups of rotational-flow separation devices are arranged on the machine frame platform is adopted, and mixed liquid of konjak powder is subjected to positive and negative step-type washing and discharging in the multiple groups of rotational-flow separation devices by a principle of multi-time washing of a washing machine, so that the purposes of efficiently removing impurities and extracting the konjak powder are achieved.
Description
Technical field
The utility model belongs to the separation equipment technical field, is specifically related to the high pressure cyclone reverse rolling continuous separation device that a kind of simple in structure, working stability is reliable, can effectively improve glucomannans content.
Background technology
Konjaku is a kind of perennial grass wood plant.Underground stem tuber is oblate spheroid, and individual large, petiole is sturdy, cylindrical, and light green has dark violet color spot, and palmately compound leaf is grown under sparse woods, has that level is hypoglycemic, a reducing blood lipid, step-down, loose poison, beauty treatment, promote blood circulation, lose weight, appetizing etc. is multi-functional.Konjaku is useful basic food, the too much people to the edible animal acid food, and konjaku is eaten in collocation, can reach food acid, soda balance, favourable to health.The folks of china plantation processing and eating konjaku history of existing more than 2000 year, but just sporadicly edible in southwest in the past, over nearly more than 20 years, along with expanding economy, the raising of people's living standard, diet has also turned to present cuisines health from the auxotype of being satiated with food in past, and the konjak food industry has had larger development.China now existing 15 provinces and regions starts scale plantation processing and eating konjaku.Also there are in the world a lot of countries to eat konjak food.Wherein, Japan contains most, on average will eat the 0.6Kg konjak food for each person every day.In the mid-90, people generally believe that Chinese Amorphophallus plantation, processing and research level fall behind at least 15 years than Japan.But recent years, government has strengthened konjaku research dynamics, and the konjaku process technology improves constantly, and various professional equipments are updated perfect, and the quality of product has also had remarkable improvement, and its application study level is maked rapid progress especially.The value of konjaku maximum is its glucomannan (KGM) composition, and konjaku is unique Main Economic crop that Glucomannan can be provided in a large number.Konjaku is extremely extensive as the purposes of food and food additives:
As thickener and stabilizing agent, can add in jelly, jam, fruit juice, vegetable juice, ice cream, ice cream and other cold drinks, solid beverage, toppings and soup stock powder; As binding agent, can add in noodles, rice noodles, strand skin, burger, ham sausage, bread and cake to strengthen biceps and to keep fresh state; Can add in various soft sweets, sticky candy and crystal sugar as gel, can also be used to make bionic foods; Colourful konjak food, will hold out broad prospects.And in the roughing process, all to use edible sulfur fumigation as the special processing process that suppresses the fresh Amorphophallus rivieri brown stain.Adopt appropriate edible alcohol and drinking water to be mixed with to suppress swollen rise press down swollen dose, then by every kilogram, contain the konjaku flour that is greater than 300 ppm sulfur dioxide and be placed in 1:4 times of solution and carry out the agitator treating desulfurization, be called for short purifying.Under routine techniques, the content of glucomannans can only reach 70% usually, and viscosity is up to 28000mpa.s, and content of sulfur dioxide is also higher.For this reason, develop and a kind ofly can effectively improve glucomannans content, the device that increases its viscosity and reduce content of sulfur dioxide is of great immediate significance.
The utility model content
The purpose of this utility model be to provide a kind of simple in structure, working stability reliable, can effectively improve the high pressure cyclone reverse rolling continuous separation device of glucomannans content.
The purpose of this utility model is to realize like this, a kind of high pressure cyclone reverse rolling continuous separation device, comprise framework platform, power distribution cabinet, continuous separation equipment rolls, the alcohol measuring container, on described framework platform, power distribution cabinet is set, continuous separation equipment and alcohol measuring container roll, the continuous separation equipment of described rolling and power distribution cabinet are electrically connected, the continuous separation equipment of described rolling comprises head tank, cyclone separation device, discharging tube, collecting pipe, waste material discharging tube and garbage collection pipe, described head tank arranges the waste material discharging tube, described waste material discharging tube is connected by cyclone separation device, described discharging tube is by the series connection of cyclone separation device interval.
The utility model takes to arrange the structure of many group cyclone separation devices on framework platform, the principle of having utilized washing of drum type washing machine repeatedly to clean, the mixing material of konjaku flour is entered in many group cyclone separation devices and carries out both forward and reverse directions ladder type washing discharge, forward direction utilizes the limpid mixing material of liquid after the ladder type washing that the proportion principle of material and solution will contain konjaku flour to be transported to the fine processing stage, to contain micro-konjaku flour, starch, impurity, alkaloidal troubled liquor enters cyclone separation device and adopts equally the proportion principle again after the ladder type washing, to carry out last cyclonic separation, reach the purpose that the micro-konjaku flour of turbid solution the inside obtains reclaiming thoroughly.The utility model also is provided with the alcohol measuring container, can regulate at any time the addition of controlling alcohol, makes in the purifies and separates process, and konjaku flour can or not exceed standard because of the not enough of alcohol amount and have influence on the quality of konjaku flour.
The accompanying drawing explanation
Fig. 1 is that the utility model overall structure master looks schematic diagram;
The schematic top plan view that Fig. 2 is Fig. 1;
Fig. 3 is that the utility model cyclone separation device is used state partly to cut open schematic diagram;
In figure: 1-framework platform, 2-power distribution cabinet, 3-head tank, 4-cyclone separation device, 5-waste material discharging tube, 6-garbage collection pipe, 7-discharging tube, 8-collecting pipe, 9-alcohol measuring container, 10-alcohol dilution adds pipeline, and 11-alcohol adds pipeline, the 12-centrifugal pump, the 13-motor.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is further described, but never in any form the utility model is limited, any conversion or the replacement based on the utility model training centre, done, all belong to protection domain of the present utility model.
As Fig. 1, shown in 2, the utility model comprises framework platform 1, power distribution cabinet 2, continuous separation equipment rolls, alcohol measuring container 9, on described framework platform 1, power distribution cabinet 2 is set, continuous separation equipment and alcohol measuring container 9 roll, the continuous separation equipment of described rolling and power distribution cabinet 2 are electrically connected, the continuous separation equipment of described rolling comprises head tank 3, cyclone separation device 4, waste material discharging tube 5, garbage collection pipe 6, discharging tube 7 and collecting pipe 8, described head tank 3 arranges discharging tube 7, described cyclone separation device 4 is connected successively by discharging tube 7, described cyclone separation device 4 is by the 5 interval series connection of waste material discharging tube.
The interior swirl stirring device that arranges of described cyclone separation device 4.
Described discharging tube 5 is arranged on position on the lower side, cyclone separation device 4 casing middle parts.
Described discharging tube 7 is arranged on cyclone separation device 4 bottoms.
Described cyclone separation device 4 connects centrifugal pump 12, and described centrifugal pump 12 is driven by motor 13.
Described cyclone separation device 4 is at least two groups.
On described collecting pipe 6, by-pass valve control is set.
The alcohol dilution is set on described alcohol measuring container 9 and adds pipeline 10 and alcohol interpolation pipeline 11, described alcohol dilution adds pipeline 10 and is connected with cyclone separation device 4 respectively with alcohol interpolation pipeline 11, on described alcohol dilution interpolation pipeline 10 and alcohol interpolation pipeline 11, by-pass valve control is set.
the purifying of konjaku flour of below take is example explanation the utility model operation principle and the course of work:
The utility model takes to arrange the structure of many group cyclone separation devices on framework platform, the principle of having utilized washing of drum type washing machine repeatedly to clean, the mixing material of konjaku flour is entered in many group cyclone separation devices and carries out both forward and reverse directions ladder type washing discharge, forward direction utilizes the limpid mixing material of liquid after the ladder type washing that the proportion principle of material and solution will contain konjaku flour to be transported to the fine processing stage, to contain micro-konjaku flour, starch, impurity, alkaloidal troubled liquor enters cyclone separation device and adopts equally the proportion principle again after the ladder type washing, to carry out last cyclonic separation, reach the purpose that the micro-konjaku flour of turbid solution the inside obtains reclaiming thoroughly.
During the utility model work: konjaku flour is placed in to the liquid the inside of containing 36% edible alcohol concentration and is stirred, immersion allows konjaku flour present the length of should splashing, both forward and reverse directions ladder type washing discharge is carried out in the cyclone separation device the inside that again can not expanded mixing material enters many group arranged types, forward direction is along discharging tube (7) to collecting pipe (8) direction, utilize the limpid mixing material of liquid after the ladder type washing that the proportion principle of material and solution will contain konjaku flour to be transported to the fine processing stage, reverse directions is along waste material discharging tube (5) to garbage collection pipe (6) direction, to contain micro-konjaku flour, starch, impurity, alkaloidal troubled liquor enters cyclone separation device, the same proportion principle that adopts is carried out last cyclonic separation after the ladder type washing, the micro-konjaku flour that reaches the turbid solution the inside is reclaimed thoroughly.The alcohol measuring container of the utility model setting effectively reclaims the alcohol after purifying, when the alcohol amount in purge process is inadequate, open the control valve of alcohol measuring container, supply with alcohol, make konjaku flour can not produce because of the deficiency of alcohol amount expanded, affect the quality of konjaku flour.
Claims (8)
1. a high pressure cyclone reverse rolling continuous separation device, comprise framework platform (1), power distribution cabinet (2), continuous separation equipment rolls, alcohol measuring container (9), power distribution cabinet (2) is set on described framework platform (1), continuous separation equipment and alcohol measuring container (9) roll, the continuous separation equipment of described rolling and power distribution cabinet (2) are electrically connected, it is characterized in that the continuous separation equipment of described rolling comprises head tank (3), cyclone separation device (4), waste material discharging tube (5), garbage collection pipe (6), discharging tube (7) and collecting pipe (8), described head tank (3) arranges discharging tube (7), described cyclone separation device (4) is connected successively by discharging tube (7), described cyclone separation device (4) is by the series connection of waste material discharging tube (5) interval.
2. high pressure cyclone reverse rolling continuous separation device according to claim 1, is characterized in that, in described cyclone separation device (4), swirl stirring device is set.
3. high pressure cyclone reverse rolling continuous separation device according to claim 1, is characterized in that described discharging tube (5) is arranged on position on the lower side, cyclone separation device (4) casing middle part.
4. high pressure cyclone reverse rolling continuous separation device according to claim 1, is characterized in that described discharging tube (7) is arranged on cyclone separation device (4) bottom.
5. high pressure cyclone reverse rolling continuous separation device according to claim 1 and 2, is characterized in that described cyclone separation device (4) connects centrifugal pump (12), and described centrifugal pump (12) is driven by motor (13).
6. high pressure cyclone reverse rolling continuous separation device according to claim 5, is characterized in that described cyclone separation device (4) is at least two groups.
7. high pressure cyclone reverse rolling continuous separation device according to claim 1, is characterized in that, on described collecting pipe (6), by-pass valve control is set.
8. high pressure cyclone reverse rolling continuous separation device according to claim 1, it is characterized in that on described alcohol measuring container (9) arranging the alcohol dilution and add pipeline (10) and alcohol interpolation pipeline (11), described alcohol dilution adds pipeline (10) and is connected with cyclone separation device (4) respectively with alcohol interpolation pipeline (11), on described alcohol dilution interpolation pipeline (10) and alcohol interpolation pipeline (11), by-pass valve control is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320348693 CN203342963U (en) | 2013-06-18 | 2013-06-18 | High-pressure rotational-flow reverse-rolling continuous separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320348693 CN203342963U (en) | 2013-06-18 | 2013-06-18 | High-pressure rotational-flow reverse-rolling continuous separation device |
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| Publication Number | Publication Date |
|---|---|
| CN203342963U true CN203342963U (en) | 2013-12-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320348693 Expired - Fee Related CN203342963U (en) | 2013-06-18 | 2013-06-18 | High-pressure rotational-flow reverse-rolling continuous separation device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103357525A (en) * | 2013-06-18 | 2013-10-23 | 昭通市三艾有机魔芋发展有限责任公司 | High-pressure cyclone reverse-rolling continuous separation device |
-
2013
- 2013-06-18 CN CN 201320348693 patent/CN203342963U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103357525A (en) * | 2013-06-18 | 2013-10-23 | 昭通市三艾有机魔芋发展有限责任公司 | High-pressure cyclone reverse-rolling continuous separation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131218 Termination date: 20180618 |
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| CF01 | Termination of patent right due to non-payment of annual fee |