CN208312875U - A kind of device improving existing space division liquid yield - Google Patents
A kind of device improving existing space division liquid yield Download PDFInfo
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- CN208312875U CN208312875U CN201820920669.6U CN201820920669U CN208312875U CN 208312875 U CN208312875 U CN 208312875U CN 201820920669 U CN201820920669 U CN 201820920669U CN 208312875 U CN208312875 U CN 208312875U
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Abstract
The utility model discloses a kind of devices for improving existing space division liquid yield, comprising: ice chest is set to main heat exchanger in ice chest, Shang Ta, Xia Ta and former expanding machine, and the former supercharger and former cooler that are set to outside ice chest；It further include the plug-in supercharger being set to outside ice chest, plug-in cooler, plug-in small ice chest, in which: portion of air is connected to through main heat exchanger with the bottom of lower tower；Another part air is successively connected to through former supercharger, former cooler, main heat exchanger, former expanding machine with the middle part of upper tower；Third stock air successively converges through plug-in supercharger, plug-in cooler and the air after former chiller treatment；4th strand of air is connected to through the plug-in expanding machine in plug-in small ice chest with the middle part of upper tower.The device of the existing space division liquid yield of the raising of the utility model, makes full use of the extra production capacity of air separation plant, effectively increases the yield of space division liquid by plug-in sled block.
Description
Technical field
The utility model relates to a kind of devices for increasing space division liquid yield more particularly to a kind of improve to have space division liquid
The device of yield.
Background technique
Large Air Separation Devices in design its to meet fluctuation ability be an important technical indicator, often with maximum processing
Ability come design pipe diameter, heat exchanger heat exchange and packed tower processing capacity.In actual use, by the limit of gas consumption
Maximum value can be not achieved in system, production capacity, so equipment has part design margin when running.Cause the production capacity waste of equipment.
Therefore, those skilled in the art is dedicated to the method that exploitation increases space division liquid yield, is exactly to change
The rich production capacity of load space division is utilized to increase liquid yield, and economic value method is created.
Utility model content
There is the waste of production capacity part existing built space division in the utility model, propose that a kind of raising has been had time
Divide the device of liquid yield.
To achieve the above object, the utility model uses following technical scheme:
The utility model provides a kind of device for improving existing space division liquid yield, comprising: ice chest is set to the ice chest
Interior main heat exchanger, Shang Ta, Xia Ta and former expanding machine, and the former supercharger and former cooler that are set to outside the ice chest；Also
Including the plug-in supercharger, plug-in cooler, plug-in small ice chest being set to outside the ice chest, in which:
Portion of air is connected to through main heat exchanger with the bottom of the lower tower by pipeline；
Another part air is by pipeline successively through the former supercharger, the former cooler, the main heat exchanger, described
Former expanding machine is connected to the middle part of the upper tower；
The third stock air drawn from another part air is by pipeline successively through the plug-in supercharger, described
Plug-in cooler converges with the air after the former chiller treatment；And
Converge the extract out in air the 4th strand of air from after main heat exchanger heat exchange, by pipeline through described plug-in
Plug-in expanding machine in small ice chest is connected to the middle part of the upper tower, and the heat of generation is transmitted to institute by the plug-in expanding machine
It states outside plug-in small ice chest, the cooling capacity of generation enters in cold box system.
Further, in the device of the existing space division liquid yield of raising, the original supercharger and the original are swollen
Swollen machine passes through axis connection；The plug-in supercharger and the plug-in expanding machine pass through axis connection.
Further, in the device of the existing space division liquid yield of raising, the inlet duct of the original supercharger
It is connected to by pipeline and valve with the outlet conduit of the former cooler.
Further, in the device of the existing space division liquid yield of raising, the inlet tube of the plug-in supercharger
Road is connected to by pipeline and valve with the outlet conduit of the plug-in cooler.
Further, in the device of the existing space division liquid yield of the described raising, the plug-in small ice chest with it is described cold
Pass through connection of passing a bridge between case.
Further, in the device of the existing space division liquid yield of raising, after main heat exchanger heat exchange
Converge air to extract out from the middle part of the main heat exchanger.
Further, in the device of the existing space division liquid yield of raising, the cold box system is by plug-in small cold
Case, gap bridge and ice chest composition.
The utility model by adopting the above technical scheme, compared with prior art, has the following technical effect that
The device provided by the utility model for improving existing space division liquid yield, makes full use of the extra production of air separation plant
Can, space division liquid is increased by plug-in sled block (plug-in expanding machine, plug-in supercharger, plug-in cooler, plug-in small ice chest, gap bridge)
Yield, there is good economic benefit；And because being the extra production capacity using air separation plant, therefore to stabilization of equipment performance and space division
Other component parts of equipment etc. do not have an impact.
Detailed description of the invention
Fig. 1 is a kind of flow diagram for the device for improving existing space division liquid yield of the utility model；
Wherein, each appended drawing reference are as follows:
1- ice chest；2- heat exchanger；The upper tower of 3-；Tower under 4-；5- original supercharger；6- original cooler；7- original expanding machine；8- is plug-in
Supercharger；The plug-in cooler of 9-；The plug-in expanding machine of 10-；The plug-in small ice chest of 11-；12- passes a bridge.
Specific embodiment
The utility model is described in more detail below by specific embodiment, for a better understanding of this reality
With novel, but following embodiments are not intended to limit the scope of the utility model.
Embodiment 1
As shown in Figure 1, present embodiments providing a kind of device for improving existing space division liquid yield, comprising: ice chest 1, if
Main heat exchanger 2, upper tower 3, lower tower 4 and the former expanding machine 7 being placed in the ice chest 1, and the former increasing being set to outside the ice chest 1
Press 5 and former cooler 6；It further include the plug-in supercharger 8 being set to outside the ice chest, plug-in cooler 9, plug-in small ice chest
11, in which:
Portion of air is connected to through main heat exchanger 2 with the bottom of the lower tower 4 by pipeline；
Another part air by pipeline successively through the former supercharger 5, the former cooler 6, the main heat exchanger 2,
The original expanding machine 7 is connected to the middle part of the upper tower 3；
The third stock air drawn from another part air is by pipeline successively through the plug-in supercharger 8, institute
It states plug-in cooler 9 and the former cooler 6 treated that air converges, converge air after the main heat exchanger 2 heat exchange
It is extracted out from the middle part of the main heat exchanger 2；And
Converge the extract out in air the 4th strand of air from after the main heat exchanger 2 heat exchange, by pipeline through described outer
The plug-in expanding machine 10 hung in small ice chest 11 is connected to the middle part of the upper tower 3, and the heat of generation passes through the plug-in expanding machine
10 are transmitted to outside the plug-in small ice chest 11, and the cooling capacity of generation enters in cold box system, and the cold box system is by plug-in small ice chest
11, gap bridge 12 and ice chest 1 form, and the cooling capacity of generation, can be all to produce liquid in addition to maintaining 12 cold damages of small ice chest 11 and gap bridge.
In the present embodiment, the former supercharger 5 passes through axis connection with the former expanding machine 7；The plug-in supercharger 8 with
The plug-in expanding machine 10 passes through axis connection.
In the present embodiment, the inlet duct of the former supercharger 5 going out by pipeline and valve and the former cooler 6
Mouth pipeline connection.The inlet duct of the plug-in supercharger 8 passes through the outlet conduit of pipeline and valve and the plug-in cooler 9
Connection.
Embodiment 2
A kind of application for the device for improving existing space division liquid yield of the present embodiment, existing built space division generally comprise:
Ice chest 1, main heat exchanger 2, former supercharger 5, former expanding machine 7, upper tower 3, lower tower 4, as shown in Figure 1, and former supercharger 5 expanded with former
Machine 7 passes through axis connection.
The process flow of existing apparatus are as follows: air through the leading portions such as overcompression, pre-cooling, purifying processing after, pipeline GA-101's
Pressure is~0.45MPaG, and temperature is~12-17 DEG C.Get rid of contained almost all carbon dioxide, water and part hydrocarbonization
After closing object, it is divided into two parts.A part of GA-101 enters the main heat exchanger 2 in ice chest 1, after being cooled to liquefaction point, through pipeline GA-
102 enter lower tower 4.Another part GA-201 enters supercharger 5 and is compressed to 0.6~0.8MPaG, recycles the function of expanding machine release,
~40 DEG C are cooled to using cooler 6, passes through pipeline GA-202.The main heat exchanger 2 being sent into ice chest 1, from main heat exchanger 2
Portion extraction, by pipeline GA-204 extract out when temperature be -110 DEG C~-140 DEG C, into expanding machine 7 be expanded to pressure 0.01~
0.05MPa, temperature are -175~-185 DEG C, and by pipeline GA-205, tower 3 participates in rectifying in feeding.The expansion process of expanding machine 7
It is the process externally done work using gas internal energy, by the rotation of expanding machine, expanding end high pressure (0.6~0.8MPaG) height
The gas energy of temperature (- 110 DEG C~-140 DEG C) transfers out, and air itself is depressured (0.01~0.05MPa) cooling (- 175
~-185 DEG C).Using entire ice chest as research system, the heat in ice chest 2 mainly passes through expanding machine 7 and is transmitted to outside ice chest, heat
Outflow be exactly cooling capacity generation process.The cooling capacity part of generation maintains the thermal losses of ice chest, remainder to liquefied gas,
Generate liquefied oxygen or nitrogen.
Since varying duty space division designs pipeline, heat exchanger and rectifying column in design with maximum tolerance in existing apparatus
Tolerance is handled, in underload, flow velocity is relatively low in pipeline, and heat exchanger channel has part rich, and the load of rectifying column can also compare
It is low.It is transformed based on this: drawing one air (~23000Nm from air into machine preceding pipeline GA-201 is increased3/ h) into
Entering pipeline GA-301, is pressurized into plug-in supercharger 8, air can be pressurized (0.6~0.8MPaG) heating (30~80 DEG C), then
After being cooled to~40 DEG C by cooler 9, pipeline GA-202 after former supercharger is entered by GA-302, is sent into main heat exchange after merging
Device 2.In order to copy the surge of plug-in supercharger, pipeline GA-302 is connected to GA-301 by GA-303 pipeline, passes through adjusting
Valve is controlled, and plays the role of protecting supercharger.The gas piping GA-204 extracted out in the middle part of main heat exchanger 2 meets branch GA-
304, take out portion of air (~23000Nm3/ h) by gap bridge 12, it is sent into plug-in expanding machine 10 and expands, air itself is depressured
(0.01~0.05MPa) cools down (- 175~-185 DEG C).Heat is transmitted to outside ice chest by plug-in expanding machine 10, corresponding generation
Cooling capacity enters the cold box system being made of plug-in small ice chest 11,12, ice chest 1 of passing a bridge.The cooling capacity of generation is except small 11 He of ice chest of maintenance
It passes a bridge outside 12 cold damages, it can be all to produce liquid.23000Nm3The tolerance of/h can increase cooling capacity about 300~400kw, can increase
Liquid yield, in terms of liquid oxygen: 3~3.7t/h.Generate considerable economic benefit.
The present embodiment utilizes the extra production capacity of air separation plant, by plug-in sled block (containing expanding machine, supercharger, cooler, small
Ice chest, gap bridge) effectively increase the yield of space division liquid；Moreover, because being the extra production capacity using air separation plant, therefore to equipment
Other component parts (such as: argon system, rare gas system) of stability and air separation plant etc. do not have an impact.
Specific embodiment of the utility model is described in detail above, but it is merely an example, this is practical new
Type is not restricted to particular embodiments described above.To those skilled in the art, any pair of the utility model carries out
Equivalent modifications and substitution also all among the scope of the utility model.Therefore, in the spirit and model for not departing from the utility model
Lower made equal transformation and modification are enclosed, should all be covered in the scope of the utility model.
Claims (7)
1. a kind of device for improving existing space division liquid yield, comprising: ice chest (1), the main heat exchange being set in the ice chest (1)
Device (2), upper tower (3), lower tower (4) and former expanding machine (7), and it is set to the outer former supercharger (5) of the ice chest (1) and original is cold
But device (6)；It is characterized in that, further including the plug-in supercharger (8) being set to outside the ice chest, plug-in cooler (9), plug-in small
Ice chest (11), in which:
Portion of air is connected to through main heat exchanger (2) with the bottom of the lower tower (4) by pipeline；
Another part air is by pipeline successively through the former supercharger (5), the former cooler (6), the main heat exchanger
(2), the former expanding machine (7) is connected to the middle part of the upper tower (3)；
The third stock air drawn from another part air is by pipeline successively through the plug-in supercharger (8), described
Treated, and air converges plug-in cooler (9) with the former cooler (6)；And
Converge the extract out in air the 4th strand of air from after the main heat exchanger (2) heat exchange, by pipeline through described plug-in
Plug-in expanding machine (10) in small ice chest (11) is connected to the middle part of the upper tower (3), and the heat of generation passes through described plug-in swollen
Swollen machine (10) is transmitted to the plug-in small ice chest (11) outside, and the cooling capacity of generation enters in ice chest device.
2. the device according to claim 1 for improving existing space division liquid yield, which is characterized in that the original supercharger
(5) pass through axis connection with the former expanding machine (7)；The plug-in supercharger (8) and the plug-in expanding machine (10) are connected by axis
It connects.
3. the device according to claim 1 for improving existing space division liquid yield, which is characterized in that the original supercharger
(5) inlet duct is connected to by pipeline and valve with the outlet conduit of the former cooler (6).
4. the device according to claim 1 for improving existing space division liquid yield, which is characterized in that the plug-in supercharger
(8) inlet duct is connected to by pipeline and valve with the outlet conduit of the plug-in cooler (9).
5. the device according to claim 1 for improving existing space division liquid yield, which is characterized in that the plug-in small ice chest
(11) it is connected between the ice chest (1) by gap bridge (12).
6. the device according to claim 1 for improving existing space division liquid yield, which is characterized in that through the main heat exchanger
(2) air that converges after exchanging heat is extracted out from the middle part of the main heat exchanger (2).
7. the device according to claim 1 for improving existing space division liquid yield, which is characterized in that cold box system is by plug-in
Small ice chest (11), gap bridge (12) and ice chest (1) composition.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820920669.6U CN208312875U (en) | 2018-06-14 | 2018-06-14 | A kind of device improving existing space division liquid yield |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201820920669.6U CN208312875U (en) | 2018-06-14 | 2018-06-14 | A kind of device improving existing space division liquid yield |
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| CN208312875U true CN208312875U (en) | 2019-01-01 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108413708A (en) * | 2018-06-14 | 2018-08-17 | 上海联风能源科技有限公司 | It is a kind of to improve the method and device for having space division liquid yield |
-
2018
- 2018-06-14 CN CN201820920669.6U patent/CN208312875U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108413708A (en) * | 2018-06-14 | 2018-08-17 | 上海联风能源科技有限公司 | It is a kind of to improve the method and device for having space division liquid yield |
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