CN205512099U

CN205512099U - System for preparation F55 fructose

Info

Publication number: CN205512099U
Application number: CN201620068149.8U
Authority: CN
Inventors: 王建东
Original assignee: Lu Zhou Biotechnology (sichuan) Co Ltd
Current assignee: Lu Zhou Biotechnology (sichuan) Co Ltd
Priority date: 2016-01-25
Filing date: 2016-01-25
Publication date: 2016-08-31
Anticipated expiration: 2026-01-25

Abstract

The utility model discloses a system for preparation F55 fructose, it is including saccharification jar (4) connected in order, rotary drum filter (5), pump a (6), neutralization decoloration jar A (7), closed filter A (8), cloth envelop collector A (9), from handing over ware A (10), different structure post (11), pump b (12), neutralization decoloration jar B (13), closed filter B (14), cloth envelop collector B (15) and from handing over ware B (16), be connected with in order between evaporative concentration ware I's (1) exit end F and evaporative concentration ware II's (2) the entry end E pump c (17), chromatographic column (18), neutralization decoloration jar C (19), closed filter C (20), sack formula filter C (21) and from handing over ware C (22). The beneficial effects of the utility model are that: easy operation, degree of automation height, the preparation that can realize 75%F42 fructose and F55 fructose simultaneously, production efficiency height.

Description

A kind of system preparing F55 fructose

Technical field

This utility model relates to the use of Semen Maydis and prepares the technical field of fructose, a kind of system preparing F55 fructose.

Background technology

Fructose can change into glycogen human body metabolism, has the effect protected the liver.Due to fructose in human body strong with cell bonding energy power, the stable effect progressively released energy can be played, therefore the effect of muscle power allaying tiredness can be kept.Fructose metabolism does not produce lactic acid, vivo protein consumption, body endurance and metabolic effects can also be suppressed, be therefore very suitable for preparing the functional drink product of supplementary physical ability, using the nutrient as athlete and physical labourer, it is also possible to the nutrient source regained one's strength as baby, anemia of pregnant woman.Additionally, fructose is also to surgical site infections, supplementing the loss of albumen, gastritis, gastric ulcer, dermatosis, dysplasia have certain effect.

Fructose injection and glucose injection effect in terms of body energy supply is suitable, but fructose injection has the advantage that blood glucose fluctuation amplitude is little, there is bigger Clinical practice be worth, and it is written into the pharmacopeia such as American and Britain, moral, day, such as Glycerin Fructose transfusion, fructose sodium chloride injection and fructose Vc tablet etc., have been used for the treatment of cardiovascular diseases, diabetes and liver etc..

Before insulin is invented, fructose was once used for treating diabetes, because fructose elimination factor is fast, blood glucose will not be caused substantially to fluctuate, and fructose can accelerate the metabolism of ethanol, may be used for treating ethylism.Fructose can be also used for treating habitual constipation, have received good clinical effectiveness.Additionally fructose also has important effect to the reproduction activity of the mankind and other mammal.

Fructose is the nutritive sweetener material sweeter than sucrose.As with sweetness of cane sugar for 100, then the sugariness of fructose is 150, and glucose sugariness is 70.The preparation of fructose is generally made with Semen Maydis for raw material material, and its preparation technology is: makes glucose through enzyme liquefaction, enzyme glycolysis, then through enzymatic conversion, part glucose is isomerized to fructose, can be made into the high fructose syrup containing fructose 42%.As separated by 42% syrup, 90% fructose can be obtained, can be in harmonious proportion and become 55% high fructose syrup.The latter is referred to as second filial generation fructose.Under same solid substrate concentration, 42% high fructose syrup sugariness is equal with sucrose, and 55% syrup sugariness is high by 10%.At present, the device structure of existing preparation 55% fructose and 42% fructose is complicated, causes preparation technology flow process loaded down with trivial details, and fructose yields poorly down, is difficult to meet consumer demand, does not promotes the use of.

Utility model content

The purpose of this utility model is to overcome the shortcoming of prior art, it is provided that a kind of compact conformation, simple to operate, automaticity is high, can realize 75%F42 fructose and the preparation of F55 fructose, the system preparing F55 fructose that production efficiency is high simultaneously.

nullThe purpose of this utility model is achieved through the following technical solutions: a kind of system preparing F55 fructose，It includes evaporation concentrator I、Evaporation concentrator II and ejector，It has been sequentially connected with saccharifying tank between the arrival end E of described ejector and evaporation concentrator I、Rotary drum filter、Pump a、Neutralize bleacher A、Closed filtering machine A、Cloth envelop collector A、From handing over device A、Isomery post、Pump b、Neutralize bleacher B、Closed filtering machine B、Cloth envelop collector B and from hand over device B，It has been sequentially connected with pump c between the port of export F and the arrival end E of evaporation concentrator II of described evaporation concentrator I、Chromatographic column、Neutralize bleacher C、Closed filtering machine C、Cloth-bag type filter C and from hand over device C，Described neutralization bleacher A、Neutralize and be respectively connected with activated carbon inlet tube on bleacher B and neutralization bleacher C.

Described from handing over device A, from handing over device B and from handing over device C to be formed by cation exchange resin and anion exchange resin, described cation exchange resin is connected with anion exchange resin.

The port of export G of described evaporation concentrator I connects the collecting tank for collecting 75%F42 fructose.

This utility model has the advantage that (1) this utility model can not only realize the preparation of 75%F90 fructose, also achieves the preparation of F55 fructose, it is achieved that the consecutive production of fructose, greatly improves production yields.(2) this utility model passes through closed filtering machine and the multistage filtering of cloth envelop collector, greatly ensure that the purity of product, meets the demand in market.(3) traditional technique is compared in whole technological process, has feature simple to operate, it is easy to achieve and automatically control.

Accompanying drawing explanation

Fig. 1 is structural representation of the present utility model；

In figure, 1-evaporation concentrator I, 2-evaporation concentrator II, 3-ejector, 4-saccharifying tank, 5-rotary drum filter, 6-pump a, with bleacher A, 8-closed filtering machine A in 7-, 9-cloth envelop collector A, 10-are from handing over device A, 11-isomery post, 12-pump b, with bleacher B, 14-closed filtering machine B in 13-, 15-cloth envelop collector B, 16-is from handing over device B, 17-pump c, 18-chromatographic column, with bleacher C in 19-, 20-closed filtering machine C, 21-cloth-bag type filter C, 22-are from handing over device C, 23-activated carbon inlet tube, 24-collecting tank.

Detailed description of the invention

Being further described this utility model below in conjunction with the accompanying drawings, protection domain of the present utility model is not limited to the following stated:

As shown in Figure 1, a kind of system preparing F55 fructose, it includes evaporation concentrator I1, evaporation concentrator II2 and ejector 3, be sequentially connected with between described ejector 3 and the arrival end E of evaporation concentrator I1 saccharifying tank 4, rotary drum filter 5, pump a6, neutralize bleacher A7, closed filtering machine A8, cloth envelop collector A9, from hand over device A10, isomery post 11, pump b12, neutralize bleacher B13, closed filtering machine B14, cloth envelop collector B15 and from hand over device B16.As shown in Figure 1, it is sequentially connected with pump c17, chromatographic column 18 between the port of export F and the arrival end E of evaporation concentrator II2 of evaporation concentrator I1, has neutralized bleacher C19, closed filtering machine C20, cloth-bag type filter C21 and be respectively connected with activated carbon inlet tube 23 on friendship device C22, described neutralization bleacher A7, neutralization bleacher B13 and neutralization bleacher C19.

As shown in Figure 1, from handing over device A10, from handing over device B16 and from handing over device C22 to be formed by cation exchange resin and anion exchange resin, described cation exchange resin is connected with anion exchange resin, is connected the cation that can filter in material and anion with anion exchange resin by cation exchange resin.

As it is shown in figure 1, the port of export G of evaporation concentrator I1 connects the collecting tank 24 for collecting 75%F42 fructose, output 60%F42 fructose at the port of export F of evaporation concentrator I.

The processing step that native system prepares F55 fructose is as follows:

S1, take the Semen Maydis after cleaning, take out the starch in Semen Maydis, by ejector 3, starch is sprayed in saccharifying tank 4, in saccharifying tank 4, add amylase and saccharifying enzyme, amylase and Glucoamylase hydrolysis starch simultaneously；

S2, the filtering of albumen, by the slurry suction rotary drum filter 5 in saccharifying tank 4, the albumen in slurry is filtered out by rotary drum filter 5 by fiber cloth, it is achieved thereby that the filtering of albumen in slurry；

S3, startup pump a6, pump a6 by the most neutralized for the slurry in rotary drum filter 5 bleacher A7, closed filtering machine A8, cloth envelop collector A9, from hand over device A10 last suction isomery post 11, wherein neutralizing bleacher A7 utilizes activated carbon by de-for slurry green grass or young crops, closed filtering machine A8 slightly walks and filters the activated carbon mixed in the slurry, cloth envelop collector A9 deeper into filter and mix activated carbon in the slurry, from handing over device A10 to filter the zwitterion in slurry, and slurry is converted to F42 fructose by isomery post 11；

nullS4、75%F42 fructose and the preparation of 60%F42 fructose，Start pump b12，Pump b12 is by the most neutralized for the fructose in isomery post 11 bleacher B13、Closed filtering machine B14、Cloth envelop collector B15、From handing over device B16 last suction evaporation concentrator I1，Wherein neutralizing bleacher B13 utilizes activated carbon by de-for slurry green grass or young crops，Closed filtering machine B14 slightly walks and filters the activated carbon mixed in the slurry，Cloth envelop collector B15 deeper into filter and mix activated carbon in the slurry，The zwitterion in slurry is filtered from handing over device B16，35%F42 fructose is being prepared in handing over device B16，And prepare 75%F42 fructose at the port of export G of evaporation concentrator I1，60%F42 fructose is prepared at the port of export F of evaporation concentrator I1，It is achieved thereby that 75%F42 fructose and the preparation of 60%F42 fructose；

S5, the preparation of 75%F90 fructose, start pump c17, pump c17 by 60%F42 fructose sequentially through chromatographic column 18, neutralize bleacher C19, closed filtering machine C20, cloth-bag type filter C21, in handing over device C22 last suction evaporation concentrator II2, wherein 60%F42 fructose is converted to 30%F90 fructose by chromatographic column 18, neutralizing bleacher C19 utilizes activated carbon by de-for slurry green grass or young crops, closed filtering machine C20 slightly walks and filters the activated carbon mixed in the slurry, cloth envelop collector C deeper into filter and mix activated carbon in the slurry, the zwitterion in slurry is filtered from handing over device C22, and in evaporation concentrator II2, prepare 75%F90 fructose, it is achieved thereby that the preparation of 75%F90 fructose；

The preparation of S6, F55 fructose, takes out 75%F90 fructose and 75%F42 fructose mixes according to a certain percentage, it is achieved thereby that the preparation of F55 fructose.Therefore, not only achieve the preparation of 75%F90 fructose, also achieve the preparation of F55 fructose, it is achieved that the consecutive production of fructose, greatly improve production yields；By closed filtering machine and the multistage filtering of cloth envelop collector, greatly ensure that the purity of product, meet the demand in market, additionally, traditional technique is compared in whole technological process, there is feature simple to operate, it is easy to achieve and automatically control.

The above is only preferred implementation of the present utility model, it is to be understood that this utility model is not limited to form disclosed herein, it is not to be taken as the eliminating to other embodiments, and can be used for other combinations various, amendment and environment, and can be modified by above-mentioned teaching or the technology of association area or knowledge in contemplated scope described herein.And the change that those skilled in the art are carried out and change are without departing from spirit and scope of the present utility model, the most all should be in the protection domain of this utility model claims.

Claims

null1. the system preparing F55 fructose，It is characterized in that: it includes evaporation concentrator I(1)、Evaporation concentrator II(2) and ejector (3)，Described ejector (3) and evaporation concentrator I(1) arrival end E between be sequentially connected with saccharifying tank (4)、Rotary drum filter (5)、Pump a(6)、Neutralize bleacher A(7)、Closed filtering machine A(8)、Cloth envelop collector A(9)、From handing over device A(10)、Isomery post (11)、Pump b(12)、Neutralize bleacher B(13)、Closed filtering machine B(14)、Cloth envelop collector B(15) and from handing over device B(16)，Described evaporation concentrator I(1) port of export F and evaporation concentrator II(2) arrival end E between be sequentially connected with pump c(17)、Chromatographic column (18)、Neutralize bleacher C(19)、Closed filtering machine C(20)、Cloth-bag type filter C(21) and from handing over device C(22)，Described neutralization bleacher A(7)、Neutralize bleacher B(13) and neutralization bleacher C(19) on be respectively connected with activated carbon inlet tube (23).
A kind of system preparing F55 fructose the most according to claim 1, it is characterized in that: described from handing over device A(10), from handing over device B(16) and from handing over device C(22) formed by cation exchange resin and anion exchange resin, described cation exchange resin is connected with anion exchange resin.
A kind of system preparing F55 fructose the most according to claim 1, it is characterised in that: port of export G described evaporation concentrator I(1) connects the collecting tank (24) for collecting 75%F42 fructose.