Circulating sugar manufacturing facility

A cyclic and equipment technology, applied in sugar production, sugar production, fructose production and other directions, can solve the problems of increasing production cost, easy formation of acid mist, tank corrosion, etc., to save production cost and achieve good heating effect. , the effect of improving productivity

Inactive Publication Date: 2017-03-29
陈彦羽
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The agitator needs a motor to drive, and the material liquid that reaches the appropriate pH value after stirring also needs a discharge motor, which wastes a lot of energy consumption
The PH adjustment tank generally adopts a 10 cubic stainless steel tank, which is relatively large in volume. Moreover, afte

Method used

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  • Circulating sugar manufacturing facility
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Embodiment Construction

[0018] The technical solution of this patent will be further described in detail below in conjunction with specific embodiments.

[0019] see Figure 1-2 , a circulating sugar production equipment, including a maintenance tank 1, an acid tank 4, a secondary flash tank 3, a buffer tank 6, a glucoamylase tank 8 and a saccharification tank 11; The liquid is injected into the secondary flash tank 3, and the discharge port of the maintenance tank 1 is connected to the feed port of the first water pump 2, and the discharge port of the first water pump 2 is connected to the feed port of the secondary flash tank 3; The discharge port at the bottom of the secondary flash tank 3 is connected to the feed port at the top of the buffer tank 6, wherein the acid tank 4 is connected to the vacuum pump 5, and the vacuum pump 5 is connected to the top of the buffer tank 6; the buffer tank 6 is provided with a liquid level gauge, and the buffer tank There is a liquid level gauge port on the sid...

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Abstract

The invention discloses a circulating sugar manufacturing facility which comprises a maintenance tank, an acid tank, a double-flash evaporation tank, a buffer tank, a saccharifying enzyme tank and a saccharifying tank, wherein the maintenance tank is injected into the double-flash evaporation tank through a first water pump, a discharge port of the maintenance tank is connected with a feed port of the first water pump, and a discharge port of the first water pump is connected with a feed port of the double-flash evaporation tank; a discharge port on the bottom of the double-flash evaporation tank is connected with a feed port on the top of the buffer tank; the acid tank is connected with a vacuum pump, and the vacuum pump is connected with the top of the buffer tank; the buffer tank is provided with a liquidometer, the side part of the buffer tank is provided with a liquidometer port, and the liquidometer penetrates into the buffer tank body through the liquidometer port; a discharge port on the bottom of the buffer tank is provided with a first valve and connected with a feed port of a second water pump through a pipeline; and a discharge port of the saccharifying enzyme tank is provided with a second valve. The circulating sugar manufacturing facility has the advantages of long service life and low production cost, increases the saccharification speed, enhances the yield, and saves both time and labor.

Description

technical field [0001] The invention relates to sugar-making equipment, in particular to a circulating sugar-making equipment. Background technique [0002] Fructose syrup is a mixture obtained by using high-quality starch as raw material, liquefied by α-amylase, saccharified by glucose, decolorized, filtered, separated and refined, and converted into fructose by immobilized isomerase. syrup. [0003] The production process of fructose syrup is: starch, pulping, liquefaction, saccharification, decolorization and filtration once, ion exchange once, evaporation concentration once, isomerization, ion exchange twice, evaporation concentration twice, chromatographic separation-, decolorization filtration three times , three times of ion exchange, three times of evaporation and concentration, and filling; [0004] Before the saccharification process, the feed liquid needs to be liquefied by two consecutive sprays, and the pH value of the feed liquid needs to be adjusted during t...

Claims

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Application Information

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IPC IPC(8): C13K11/00
CPCC13K11/00
Inventor 陈彦羽
Owner 陈彦羽
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