CN206847428U - A kind of new type of compression gas cooling system - Google Patents
A kind of new type of compression gas cooling system Download PDFInfo
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- CN206847428U CN206847428U CN201720698323.1U CN201720698323U CN206847428U CN 206847428 U CN206847428 U CN 206847428U CN 201720698323 U CN201720698323 U CN 201720698323U CN 206847428 U CN206847428 U CN 206847428U
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Abstract
Originally it is new to be related to a kind of new type of compression gas cooling system, including deep well, silt filtering apparatus, drive water pump, chilled water tank, cooling water circulating pump, atomizer, heat exchanger tube and heat transfer cabin, chilled water tank one end is by driving water pump to be connected with deep well, the other end is interconnected by cooling water circulating pump and atomizer, wherein driving water pump is interconnected by least one silt filtering apparatus with deep well, atomizer is in heat transfer cabin, and atomizer is at least one, it is and uniform around heat transfer cabin axis, heat exchanging chamber includes carrying shell, dividing plate and mozzle, it is airtight cavity structure wherein to carry shell, its axis is distributed with horizontal plane, dividing plate is embedded in carrying shell for two totally, and carrying shell is divided into inlet chamber from top to bottom, heat exchanging chamber and discharge chamber.This new one side greatly improves the stability and reliability of equipment operation, on the other hand effectively improves the compression amount of inflating and synthesis hydrazine yield, reduces the purpose of synthesis ammonia energy consumption.
Description
Technical field
Originally it is new to be related to a kind of cooling system, more particularly to a kind of new type of compression gas cooling system.
Background technology
The temperature of high pressure semiwater gas plays vital work to synthetic job when carrying out synthetic job to ammonia at present
With, in actual production find half-water gas temperature it is relatively low when, can effectively improve ammonia synthetic job efficiency and reduce ammonia
The operating power consumption of gas synthetic job, therefore in order to realize the purpose to semiwater gas cooling, while reach reduction cooling operation fortune
The requirement of row cost, the cooling system directly as cooling water with deep well low-temperature water source is currently generally employed, but in reality
Found in use, when on the one hand heat exchange between cooling water and semiwater gas mozzle be present in current cooling system, generally existing
Contact area is small, the defects of time of contact section, is followed so as to have a strong impact on the operating efficiency of cooling operation and add cooling water
Loop system operation energy consumption and burden, on the other hand, current cooling system easily occur in deep well well water in actual motion
Silt block cooling water circulation pipeline phenomenon, so as to the serious corresponding stability of cooling water system operation, and add cold
But the labor intensity and cost of water system operation and line service, therefore this phenomenon is directed to, there is an urgent need to develop one kind
New cooling system, to meet the needs of actual use.
The content of the invention
This new purpose is to provide a kind of new type of compression gas cooling system, and the new structure is simple, using flexible side
Just, on the one hand effectively overcome cooling water that traditional cooling device generally existing obtains from deep well easily because sediment charge is big and
Equipment pipeline blockage phenomenon is caused, it is on the other hand effective so as to greatly improve the stability and reliability of equipment operation
Semiwater gas cooling operations efficiency during ammonia synthetic job is improved, the compression amount of inflating and synthesis ammonia production are improved so as to reach
Amount, reduce the purpose of synthesis ammonia energy consumption.
To achieve these goals, the utility model is to realize by the following technical solutions：
A kind of new type of compression gas cooling system, including it is deep well, silt filtering apparatus, driving water pump, chilled water tank, cold
But water-circulating pump, atomizer, heat exchanger tube and heat transfer cabin, chilled water tank one end are another by driving water pump to be connected with deep well
End is interconnected by cooling water circulating pump and atomizer, wherein driving water pump passes through at least one silt filtering apparatus and depth
Well is interconnected, and atomizer is in heat transfer cabin, and atomizer is at least one, and uniform around heat transfer cabin axis, changes
Hot chamber includes carrying shell, dividing plate and mozzle, wherein carrying shell is airtight cavity structure, its axis is distributed with horizontal plane,
Dividing plate is divided into inlet chamber, heat exchanging chamber and discharge chamber for totally two from top to bottom in carrying shell, and by carrying shell, wherein described
Inlet chamber at the top of set air inlet, discharge chamber bottom sets exhaust outlet, and air inlet and exhaust outlet are coaxially distributed with carrying shell, exchanged heat
Chamber bottom side surfaces set a water inlet, and heat exchanging chamber top side surface sets a delivery port, wherein water inlet axis and heat exchanging chamber
Axis is in 45 ° -90 ° angles, and delivery port axis is in 90 ° of angles with heat exchange cavity axis, and water inlet is followed by mozzle and cooling water
Ring pump connects, and mozzle front end is interconnected in heat exchanging chamber with atomizer, and mozzle is embedded in heat exchanging chamber inside points,
It is distributed in a ring around heat exchange cavity axis, atomizer is uniform around heat exchange cavity axis and is mutually interconnected with mozzle side surface respectively
Logical, heat exchanger tube is some, in heat exchanging chamber and with carrying shell diameter parallel distribution, heat exchanger tube both ends respectively with inlet chamber and exhaust
Chamber is interconnected.
Further, the chilled water tank is closed tank structure, if another uniform dry semiconductor system in its side wall inner surfaces
Device for cooling.
Further, the atomizer axis and carrying columella line are in 30 ° -90 ° angles.
Further, the uniform some radiating wing plates of the heat exchange pipe external surface.
Further, the heat exchanger tube is any one in linear structure and helical structure.
Further, when the heat exchanger tube is spiral tube structure, then the pitch of adjacent two heat exchanger tube is identical, and spiral shell is to opposite.
Further, when the heat exchanger tube is spiral tube structure, pitch increases step by step from top to bottom.
This new structure is simple, flexible and convenient to use, on the one hand effectively overcomes traditional cooling device generally existing from depth
The cooling water obtained in well easily because sediment charge is big and caused by equipment pipeline blockage phenomenon, so as to greatly improve equipment fortune
Capable stability and reliability, semiwater gas cooling operations efficiency during ammonia synthetic job is on the other hand effectively raised,
The compression amount of inflating and synthesis hydrazine yield are improved so as to reach, reduces the purpose of synthesis ammonia energy consumption.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention.
Embodiment
Technical scheme is described further below in conjunction with the accompanying drawings.
A kind of new type of compression gas cooling system as shown in Figure 1, including deep well 1, silt filtering apparatus 2, driving water pump
3rd, chilled water tank 4, cooling water circulating pump 5, atomizer 6, heat exchanger tube 7 and heat transfer cabin 8, the one end of chilled water tank 4 is by driving water
Pump 3 is connected with deep well 1, and the other end is interconnected by cooling water circulating pump 3 and atomizer 6, wherein driving water pump 3 passes through
At least one silt filtering apparatus 2 is interconnected with deep well 1, and atomizer is in heat transfer cabin 8, and atomizer 6 is at least
One, and it is uniform around the axis of heat transfer cabin 8.
In the present embodiment, described heat exchanging chamber 8 includes carrying shell 81, dividing plate 82 and mozzle 83, wherein carrying shell 81 is
Airtight cavity structure, its axis and horizontal plane distribution, dividing plate 82 are embedded in carrying shell 81 for two totally, and by carrying shell 81 certainly
Inlet chamber 9, heat exchanging chamber 10 and discharge chamber 11 are divided under above, the wherein top of inlet chamber 9 sets air inlet 84, the bottom of discharge chamber 11
If exhaust outlet 85, air inlet 84 and exhaust outlet 85 are coaxially distributed with carrying shell 81, and the bottom side surfaces of heat exchanging chamber 10 set one and entered
The mouth of a river 86, the top side surface of heat exchanging chamber 10 set a delivery port 87, wherein the axis of water inlet 86 and the axis of heat exchanging chamber 10 in 45 °-
90 ° of angles, the axis of delivery port 86 and the axis of heat exchanging chamber 10 are in 90 ° of angles, and water inlet 86 passes through mozzle 83 and cooling water circulation
Pump 5 connects, and the front end of mozzle 83 is interconnected in heat exchanging chamber 10, and with atomizer 6, and mozzle 83 is embedded in heat exchanging chamber 10
Inside points, be distributed in a ring around the axis of heat exchanging chamber 10, atomizer 6 it is uniform around the axis of heat exchanging chamber 10 and respectively with mozzle
83 side surfaces are interconnected, and heat exchanger tube 7 is some, are distributed in heat exchanging chamber 10 and with the carrying diameter parallel of shell 81,7 liang of heat exchanger tube
End is interconnected with inlet chamber 9 and discharge chamber 11 respectively.
In the present embodiment, the chilled water tank 4 is closed tank structure, if another uniform dry semiconductor in its side wall inner surfaces
Refrigerating plant 12.
In the present embodiment, the axis of atomizer 6 is in 30 ° -90 ° angles with the carrying axis of shell 81.
In the present embodiment, the uniform some radiating wing plates 13 of the heat exchange pipe external surface.
In the present embodiment, the heat exchanger tube 7 is any one in linear structure and helical structure.
In the present embodiment, when the heat exchanger tube 7 is spiral tube structure, then the pitch of adjacent two heat exchanger tube 7 is identical, and spiral shell is to phase
Instead.
In the present embodiment, when the heat exchanger tube 7 is spiral tube structure, pitch increases step by step from top to bottom.
This is new in the specific implementation, obtains cooling water from deep well first, cooling water is by silt filtering apparatus
Enter standby in chilled water tank after filtration, purification, when being cooled down to semiwater gas, semiwater gas is held from heat exchanger
The air inlet for carrying shell is entered in inlet chamber, and after thering is heat exchanger tube to shunt the semiwater gas in inlet chamber, along heat exchange
After pipe exchanges cooling by heat exchanging chamber and in heat exchanging chamber with cooling water heat, so as to which discharge chamber is discharged, wherein in heat exchanging
During the semiwater gas cooling of intracavitary, cold water intaking is discharged, and pass through atomizer under cooling water circulating pump driving from chilled water tank
From heat exchanging chamber bottom even spray to circular intracavitary, and cooling is being back to by delivery port after heat exchange is completed with semiwater gas
Cooling down is carried out in water pot, in case reusing.
This is new in the specific implementation, separately need to be according to being cooled down in cold water water pot in cooling procedure is carried out to semiwater gas
The water and water temperature of water, supplemented by driving water pump to obtain fresh water source from deep well.
This new structure is simple, flexible and convenient to use, on the one hand effectively overcomes traditional cooling device generally existing from depth
The cooling water obtained in well easily because sediment charge is big and caused by equipment pipeline blockage phenomenon, so as to greatly improve equipment fortune
Capable stability and reliability, semiwater gas cooling operations efficiency during ammonia synthetic job is on the other hand effectively raised,
The compression amount of inflating and synthesis hydrazine yield are improved so as to reach, reduces the purpose of synthesis ammonia energy consumption.
It should be understood by those skilled in the art that the utility model is not restricted to the described embodiments, above-described embodiment and
Simply illustrate principle of the present utility model described in specification, on the premise of the spirit and scope of the utility model is not departed from,
The utility model also has various changes and modifications, and these changes and improvements both fall within claimed the scope of the utility model
It is interior.The utility model requires protection scope is by appended claims and its equivalent thereof.
Claims (7)
- A kind of 1. new type of compression gas cooling system, it is characterised in that：Described new type of compression gas cooling system includes deep water Well, silt filtering apparatus, driving water pump, chilled water tank, cooling water circulating pump, atomizer, heat exchanger tube and heat transfer cabin, it is described By driving water pump to be connected with deep well, the other end is mutually interconnected by cooling water circulating pump with atomizer for chilled water tank one end It is logical, wherein described driving water pump is interconnected by least one silt filtering apparatus with deep well, described atomizer In heat transfer cabin, and atomizer is at least one, and uniform around heat transfer cabin axis, described heat exchanging chamber include carrying shell, Dividing plate and mozzle, wherein described carrying shell is airtight cavity structure, its axis is distributed with horizontal plane, described dividing plate Totally two are divided into inlet chamber, heat exchanging chamber and discharge chamber from top to bottom in carrying shell, and by carrying shell, wherein its described Described in inlet chamber at the top of set air inlet, discharge chamber bottom sets exhaust outlet, and described air inlet and exhaust outlet are with carrying shell Coaxial distribution, described heat exchanging chamber bottom side surfaces set a water inlet, and heat exchanging chamber top side surface sets a delivery port, wherein Water inlet axis is in 45 ° -90 ° angles with heat exchange cavity axis, and delivery port axis is in 90 ° of angles with heat exchange cavity axis, and described enters The mouth of a river is connected by mozzle with cooling water circulating pump, described mozzle front end in the heat exchanging chamber, and with atomizer phase Intercommunicated, described mozzle is embedded in heat exchanging chamber inside points, is distributed in a ring around heat exchange cavity axis, described atomizer ring Around exchanging heat cavity axis uniformly and being interconnected respectively with mozzle side surface, described heat exchanger tube is some, in heat exchanging chamber simultaneously With carrying shell diameter parallel distribution, described heat exchanger tube both ends are interconnected with inlet chamber and discharge chamber respectively.
- A kind of 2. new type of compression gas cooling system according to claim 1, it is characterised in that：The chilled water tank is close Tank structure is closed, another uniform some semiconductor cooling devices in its side wall inner surfaces.
- A kind of 3. new type of compression gas cooling system according to claim 1, it is characterised in that：The atomizer axis It is in 30 ° -90 ° angles with carrying columella line.
- A kind of 4. new type of compression gas cooling system according to claim 1, it is characterised in that：The heat exchange pipe external surface Uniform some radiating wing plates.
- A kind of 5. new type of compression gas cooling system according to claim 1, it is characterised in that：The heat exchanger tube is straight line Any one in structure and helical structure.
- A kind of 6. new type of compression gas cooling system according to claim 5, it is characterised in that：The heat exchanger tube is spiral During tubular construction, then the pitch of adjacent two heat exchanger tube is identical, and spiral shell is to opposite.
- A kind of 7. new type of compression gas cooling system according to claim 5, it is characterised in that：The heat exchanger tube is spiral During tubular construction, pitch increases step by step from top to bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720698323.1U CN206847428U (en) | 2017-06-15 | 2017-06-15 | A kind of new type of compression gas cooling system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720698323.1U CN206847428U (en) | 2017-06-15 | 2017-06-15 | A kind of new type of compression gas cooling system |
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| CN206847428U true CN206847428U (en) | 2018-01-05 |
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| CN201720698323.1U Expired - Fee Related CN206847428U (en) | 2017-06-15 | 2017-06-15 | A kind of new type of compression gas cooling system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111664728A (en) * | 2020-06-29 | 2020-09-15 | 杭州富阳东山塑料机械有限公司 | Multi-pipeline multi-layer water spraying quick air cooler and tail gas cooling method thereof |
| CN112855078A (en) * | 2021-01-19 | 2021-05-28 | 江苏天广云尚节能科技有限公司 | Flow-limiting normal-pressure hot water and heat exchange system with large-diameter heat exchange tube and control method thereof |
| CN117825114A (en) * | 2024-03-05 | 2024-04-05 | 山东神驰石化有限公司 | Reactor sampling device for propane dehydrogenation propylene production equipment |
-
2017
- 2017-06-15 CN CN201720698323.1U patent/CN206847428U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111664728A (en) * | 2020-06-29 | 2020-09-15 | 杭州富阳东山塑料机械有限公司 | Multi-pipeline multi-layer water spraying quick air cooler and tail gas cooling method thereof |
| CN112855078A (en) * | 2021-01-19 | 2021-05-28 | 江苏天广云尚节能科技有限公司 | Flow-limiting normal-pressure hot water and heat exchange system with large-diameter heat exchange tube and control method thereof |
| CN117825114A (en) * | 2024-03-05 | 2024-04-05 | 山东神驰石化有限公司 | Reactor sampling device for propane dehydrogenation propylene production equipment |
| CN117825114B (en) * | 2024-03-05 | 2024-06-11 | 山东神驰石化有限公司 | Reactor sampling device for propane dehydrogenation propylene production equipment |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180105 Termination date: 20180615 |
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| CF01 | Termination of patent right due to non-payment of annual fee |