CN214913434U - Energy-saving production equipment for corn steep liquor dry powder - Google Patents
Energy-saving production equipment for corn steep liquor dry powder Download PDFInfo
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- CN214913434U CN214913434U CN202121082840.9U CN202121082840U CN214913434U CN 214913434 U CN214913434 U CN 214913434U CN 202121082840 U CN202121082840 U CN 202121082840U CN 214913434 U CN214913434 U CN 214913434U
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- steep liquor
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Abstract
The utility model relates to an energy-conserving production facility of corn steep liquor dry powder belongs to the dry technical field of thick liquids. Comprises a spray dryer, a receiver, a dust remover, a heat exchanger and a corn steep liquor storage tank. The top of the spray dryer is provided with a corn steep liquor inlet, the bottom of the spray dryer is provided with a dry powder outlet, and the side of the spray dryer is provided with a hot air inlet; the corn steep liquor inlet is connected with the corn steep liquor storage tank through a feeding pipe; the top of the receiver is provided with an air outlet, and the side surface of the receiver is provided with a dry powder inlet; the dry powder outlet is connected with the dry powder inlet through a pipeline; the air outlet is connected with the dust remover through a pipeline; the heat exchanger is provided with a heat exchanger inlet and a heat exchanger outlet; the dust remover is connected with the inlet of the heat exchanger through a pipeline; the feed pipe passes through the heat exchanger. The utility model discloses can make full use of the hot-air among the spray dryer, after removing dust to hot-air and vapor, can heat the corn steep liquor that gets into before the spray dryer, reduce the energy consumption effectively.
Description
Technical Field
The utility model relates to a dry technical field of thick liquids, concretely relates to energy-conserving production facility of corn steep liquor dry powder.
Background
The corn steep liquor is a byproduct for preparing corn starch, contains rich soluble protein, auxin and a plurality of precursor substances, and has the solid content of about 40-50 percent. Corn steep liquor is an important raw material for preparing a culture medium and can provide an organic nitrogen source necessary for the growth of microorganisms. Because the corn steep liquor is liquid, the storage, the transportation and the like are inconvenient. Therefore, there is a need to prepare corn steep liquor as a dry powder. Most dry corn steep liquor powders are produced by spray drying, which requires a large amount of heat to be used in the production process. The drying mode has great energy consumption, and the high energy consumption leads to the rise of the production cost. There is therefore a need to find a way to reduce the energy consumption of production.
SUMMERY OF THE UTILITY MODEL
The problem that the energy consumption is big when preparing the corn steep liquor dry powder among the prior art, the utility model provides an energy-conserving production facility of corn steep liquor dry powder to solve above-mentioned problem.
An energy-saving production device of corn steep liquor dry powder comprises a spray dryer, a receiver, a dust remover, a heat exchanger and a corn steep liquor storage tank. The top of the spray dryer is provided with a corn steep liquor inlet, the bottom of the spray dryer is provided with a dry powder outlet, and the side of the spray dryer is provided with a hot air inlet; the corn steep liquor inlet is connected with the corn steep liquor storage tank through a feeding pipe; the top of the receiver is provided with an air outlet, and the side surface of the receiver is provided with a dry powder inlet; the dry powder outlet is connected with the dry powder inlet through a pipeline; the air outlet is connected with the dust remover through a pipeline; the heat exchanger is provided with a heat exchanger inlet and a heat exchanger outlet; the dust remover is connected with the inlet of the heat exchanger through a pipeline; the feed pipe passes through the heat exchanger.
Further, the corn steep liquor storage tank is provided with an interlayer; the interlayer is provided with an interlayer inlet and an interlayer outlet; the interlayer inlet is connected with the heat exchanger outlet through a pipeline; and the interlayer outlet is connected with a condensed water storage tank through a pipeline. The hot gas through the heat exchanger is condensed into hot water, and the hot water still has certain temperature, can further heat the corn steep liquor in the corn steep liquor storage tank, and the heat is fully utilized.
Further, the method comprises the following steps of; the feed pipe is arranged in the heat exchanger in a snake shape. The corn steep liquor passing through the heat exchanger can be sufficiently heated.
Further, the central axis of the heat exchanger inlet is intersected with the central axis of the feeding pipe. Thus, hot gas entering the heat exchanger is directly blown to the feeding pipe, and heating is more sufficient.
Furthermore, thermometers are arranged at the corn steep liquor inlet and the air outlet. Through the temperature of monitoring corn steep liquor entry and air outlet, the velocity of flow of adjustable corn steep liquor in time makes the corn steep liquor dry more abundant.
Further, the condensed water storage tank is connected with the sewage tank. At this time, the condensed water hardly contains harmful substances and can be directly discharged after detection.
The utility model discloses a theory of operation does: hot air entering from a hot air inlet dries corn steep liquor, and the corn steep liquor contains a large amount of moisture, is heated to become water vapor, enters a receiver along with corn steep liquor dry powder, and the dry powder is settled to the lower part of the receiver, collected to a certain amount and discharged from an outlet at the lower part of the receiver for packaging; and the steam enters the dust remover from the air outlet at the upper part, and after the dust remover absorbs dust, the steam enters the heat exchanger to heat the feeding pipe.
The utility model has the advantages that:
the utility model discloses can make full use of the hot-air among the spray dryer, after removing dust to hot-air and vapor, can heat the corn steep liquor that gets into before the spray dryer, reduce the energy consumption effectively.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, and it is obvious for those skilled in the art that other drawings can be obtained according to the drawings without creative efforts.
Fig. 1 is a schematic structural diagram of the present invention;
fig. 2 is a schematic structural diagram of the heat exchanger of the present invention.
In the figure, 1-spray dryer, 2-receiver, 3-dust remover, 4-heat exchanger, 5-corn steep liquor storage tank, 6-condensed water storage tank, 7-corn steep liquor inlet, 8-hot air inlet, 9-dry powder outlet, 10-dry powder inlet, 11-air outlet, 12-heat exchanger inlet, 13-heat exchanger outlet, 14-feeding pipe, 15-interlayer inlet and 16-interlayer outlet.
Detailed Description
In order to make the technical solutions in the present invention better understood, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, but not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts shall belong to the protection scope of the present invention.
Example 1
An energy-saving production device of corn steep liquor dry powder comprises a spray dryer 1, a receiver 2, a dust remover 3, a heat exchanger 4 and a corn steep liquor storage tank 5. The top of the spray dryer 1 is provided with a corn steep liquor inlet 7, the bottom of the spray dryer is provided with a dry powder outlet 9, and the side surface of the spray dryer is provided with a hot air inlet 8; the corn steep liquor inlet 7 is connected with the corn steep liquor storage tank 5 through a feeding pipe 14; the top of the receiver 2 is provided with an air outlet 11, and the side surface is provided with a dry powder inlet 10; the dry powder outlet 9 is connected with the dry powder inlet 10 through a pipeline; the air outlet 11 is connected with the dust remover 3 through a pipeline; the heat exchanger 4 is provided with a heat exchanger inlet 12 and a heat exchanger outlet 13; the dust remover 3 is connected with the heat exchanger inlet 12 through a pipeline; the feed line 14 passes through the heat exchanger 4.
Example 2
An energy-saving production device of corn steep liquor dry powder comprises a spray dryer 1, a receiver 2, a dust remover 3, a heat exchanger 4 and a corn steep liquor storage tank 5. The top of the spray dryer 1 is provided with a corn steep liquor inlet 7, the bottom of the spray dryer is provided with a dry powder outlet 9, and the side surface of the spray dryer is provided with a hot air inlet 8; the corn steep liquor inlet 7 is connected with the corn steep liquor storage tank 5 through a feeding pipe 14; the top of the receiver 2 is provided with an air outlet 11, and the side surface is provided with a dry powder inlet 10; the dry powder outlet 9 is connected with the dry powder inlet 10 through a pipeline; the air outlet 11 is connected with the dust remover 3 through a pipeline; the heat exchanger 4 is provided with a heat exchanger inlet 12 and a heat exchanger outlet 13; the dust remover 3 is connected with the heat exchanger inlet 12 through a pipeline; the feed pipe 14 passes through the heat exchanger 4; the feed pipe 14 is arranged in a serpentine shape in the heat exchanger 4; the central axis of the heat exchanger inlet 12 intersects the central axis of the feed pipe 14; the corn steep liquor storage tank 5 is provided with an interlayer; the interlayer is provided with an interlayer inlet 15 and an interlayer outlet 16; the interlayer inlet 15 is connected with the heat exchanger outlet 13 through a pipeline; the interlayer outlet 16 is connected with the condensed water storage tank 6 through a pipeline; the corn steep liquor inlet 7 and the air outlet 11 are provided with thermometers, and the condensed water storage tank 6 is connected with the sewage tank.
Although the present invention has been described in detail by referring to the drawings in conjunction with the preferred embodiments, the present invention is not limited thereto. Various equivalent modifications or substitutions can be made on the embodiments of the present invention by those skilled in the art without departing from the spirit and substance of the present invention, and these modifications or substitutions are intended to be within the scope of the present invention/any person skilled in the art can easily conceive of changes or substitutions within the technical scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope of the claims.
Claims (6)
1. An energy-saving production device of corn steep liquor dry powder is characterized by comprising a spray dryer, a receiver, a dust remover, a heat exchanger and a corn steep liquor storage tank; the top of the spray dryer is provided with a corn steep liquor inlet, the bottom of the spray dryer is provided with a dry powder outlet, and the side of the spray dryer is provided with a hot air inlet; the corn steep liquor inlet is connected with the corn steep liquor storage tank through a feeding pipe; the top of the receiver is provided with an air outlet, and the side surface of the receiver is provided with a dry powder inlet; the dry powder outlet is connected with the dry powder inlet through a pipeline; the air outlet is connected with the dust remover through a pipeline; the heat exchanger is provided with a heat exchanger inlet and a heat exchanger outlet; the dust remover is connected with the inlet of the heat exchanger through a pipeline; the feed pipe passes through the heat exchanger.
2. An apparatus for energy efficient production of dry corn steep liquor as claimed in claim 1, wherein said feed pipe is disposed in a serpentine shape in said heat exchanger.
3. An apparatus for energy efficient production of dry corn steep liquor as claimed in claim 1, wherein the central axis of said heat exchanger inlet intersects the central axis of said feed tube.
4. An energy efficient production facility for dry corn steep liquor as claimed in claim 1, wherein said inlet and outlet ports are provided with thermometers.
5. An energy efficient production facility of corn steep liquor dry powder as claimed in claim 1, wherein said corn steep liquor storage tank is provided with an interlayer; the interlayer is provided with an interlayer inlet and an interlayer outlet; the interlayer inlet is connected with the heat exchanger outlet through a pipeline; and the interlayer outlet is connected with a condensed water storage tank through a pipeline.
6. An energy efficient production plant of corn steep liquor dry powder as claimed in claim 5, characterized in that said condensed water storage tank is connected to a sewage tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121082840.9U CN214913434U (en) | 2021-05-20 | 2021-05-20 | Energy-saving production equipment for corn steep liquor dry powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121082840.9U CN214913434U (en) | 2021-05-20 | 2021-05-20 | Energy-saving production equipment for corn steep liquor dry powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214913434U true CN214913434U (en) | 2021-11-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121082840.9U Active CN214913434U (en) | 2021-05-20 | 2021-05-20 | Energy-saving production equipment for corn steep liquor dry powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214913434U (en) |
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2021
- 2021-05-20 CN CN202121082840.9U patent/CN214913434U/en active Active
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