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Fermented feed drying method

A technology of fermented feed and drying method, which is applied in the direction of feed, dryer combination, and drying solid materials. It can solve the problems of material sticking to the pipe wall, long drying time, and uneven heating, so as to avoid sticking pipes, Good drying effect, even heating effect

Active Publication Date: 2014-02-12
MYANDE GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Because the fresh fermented feed is relatively humid, when the tube dryer is used for drying, it is easy for the material to stick to the tube wall, resulting in local overheating, uneven heating, and poor overall thermal efficiency; and because the temperature of the heat source medium steam of the tube dryer Relatively high, fermented feed products generally have low activity and product denaturation problems after drying, such as the use of low-temperature steam and low production efficiency
[0005] The tower dryer uses relatively mild hot air for drying. Although it can avoid the denaturation of the fermented feed, the drying time is too long, the production efficiency is low, and the energy consumption is too high

Method used

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  • Fermented feed drying method

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Experimental program
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Effect test

Embodiment 1

[0046] The mass ratio of the sieve material entering the auxiliary feed port 1b of the feeding machine to the fresh fermented feed is 1:8, the moisture content of the fermented feed at the discharge port 2a' of the tube dryer is 20%, and the feed port of the tower dryer has a moisture content of 20%. The moisture content of the fermented feed in 4a' was 8%.

[0047] The temperature of the steam entering the steam inlet 2b of the tubular dryer is 135°C, the temperature of the condensed water at the condensed water outlet 2b' of the tubular dryer is 110°C, and the temperature of the fermented feed outlet at the outlet 2a' of the tubular dryer is 45°C; The hot air inlet temperature of the tower dryer air inlet 4b is 80°C, the exhaust air temperature of the tower dryer air outlet 4b' is 50°C, and the fermented feed outlet temperature of the tower dryer outlet 4a' is 60°C.

[0048] The exhaust air temperature of the tubular dryer 2 is 75°C, the exhaust air temperature of the waste ...

Embodiment 2

[0050] The mass ratio of the sieve material entering the auxiliary feeding port 1b of the feeding machine to the fresh fermented feed is 1:4, the moisture content of the fermented feed at the outlet 2a' of the tube dryer is 22%, and the outlet of the tower dryer The moisture content of the fermented feed in 4a' was 10%.

[0051] The temperature of the steam entering the steam inlet 2b of the tubular dryer is 138°C, the temperature of the condensed water at the condensed water outlet 2b' of the tubular dryer is 112°C, and the temperature of the fermented feed outlet at the outlet 2a' of the tubular dryer is 50°C; The hot air inlet temperature of the tower dryer air inlet 4b is 85°C, the exhaust air temperature of the tower dryer air outlet 4b' is 52°C, and the fermented feed outlet temperature of the tower dryer outlet 4a' is 65°C.

[0052] The exhaust air temperature of the tubular dryer 2 is 78°C, the exhaust air temperature of the waste heat absorption tower outlet 8a' is 57...

Embodiment 3

[0054] The mass ratio of the sieve material entering the auxiliary feed port 1b of the feeding machine to the fresh fermented feed is 3:8, the moisture content of the fermented feed at the discharge port 2a' of the tube dryer is 25%, and the discharge port of the tower dryer has a moisture content of 25%. The moisture content of the fermented feed in 4a' was 12%.

[0055] The temperature of the steam entering the steam inlet 2b of the tubular dryer is 140°C, the temperature of the condensed water at the condensed water outlet 2b' of the tubular dryer is 115°C, and the temperature of the fermented feed outlet at the outlet 2a' of the tubular dryer is 55°C; The hot air inlet temperature of the tower dryer air inlet 4b is 90°C, the exhaust air temperature of the tower dryer air outlet 4b' is 55°C, and the fermented feed outlet temperature of the tower dryer outlet 4a' is 70°C.

[0056] The exhaust air temperature of the tubular dryer 2 is 80°C, the exhaust air temperature of the ...

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Abstract

The invention relates to a fermented feed drying method. The method comprises steps as follows in sequence: fresh fermented feed enters a feeding machine from a main feed opening, is lifted, then enters a feed opening of a tube-type drying machine, advances from front to back in the horizontal direction in the tube-type drying machine, and is subjected to indirect heat exchange with steam simultaneously; hot and humid air is exhausted by an exhaust fan from an exhaust outlet of the tube-type drying machine; the preliminarily dried fermented feed enters sieving and conveying equipment for sieving after discharged from the tube-type drying machine; after sieving, a screen underflow is sent into a feed opening in the top of a tower-type drying machine, and a screen overflow is sent into an auxiliary feed opening of the feeding machine and mixed with the fresh fermented feed; and the fermented feed moves from top to bottom in the tower-type drying machine, air enters an air inlet in the lower part of the tower-type drying machine after heated by an air heater, and hot air flows from bottom to top to perform secondary drying on the fermented feed and is exhausted from an air outlet in the upper part of the tower-type drying machine. The fermented feed drying method is low in energy consumption and high in drying efficiency, and can maintain the activity of the fermented feed.

Description

technical field [0001] The invention relates to a method for drying feed, in particular to a method for drying fermented feed. Background technique [0002] In the prior art, fluidized bed dryers, tower dryers, tube dryers, tunnel dryers, etc. are usually used to dry fermented feed. Among them, the tubular dryer uses high-temperature steam as the heat source, with high heating temperature and fast drying speed; the tower dryer uses hot air as the heat source, with low heating temperature and slow drying speed. In order to improve production efficiency, it is very common to use tubular dryers in the field of fermented feed drying. [0003] Since the fermented feed will produce a large amount of biological enzymes and other active substances, if the material temperature is higher than 70°C during the drying process (different products have different temperature resistance), the fermented feed will easily lose its activity. Therefore, the fermented feed is a heat-sensitive mat...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F26B20/00F26B3/00F26B21/00F26B25/00A23N17/00
Inventor 常寨成郝祥生冯纪网韩晓星
Owner MYANDE GRP CO LTD
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