1. A main cooling method for realizing rapid cooling of an air separation plant is characterized by comprising the following steps:

firstly, conveying nitrogen from a lower tower of a distillation tower (9) to a second heat exchange channel (13) of each layer of heat exchange device (1); the liquid oxygen flows downwards from the upper layer of the distillation tower (9) and flows into a liquid oxygen tank (10) of a heat exchange device (1) at the uppermost layer of the main cooling system;

secondly, part of the liquid oxygen flows into an overflow groove (11) below from the liquid outlet channel (101), and the liquid oxygen overflows from the top of the overflow groove and flows into a first heat exchange channel (12) below after the overflow groove is filled with the liquid oxygen;

thirdly, partial evaporation of the liquid oxygen in the first heat exchange channel (12) is carried out heat exchange with the nitrogen in the second heat exchange channel (13), so that the nitrogen is liquefied to form liquid nitrogen;

step four, the liquid oxygen in the liquid oxygen tank at the uppermost layer rises to the position of the first overflow hole (102), flows out of the first overflow hole, flows into the inflow port (91) at the lower part through the first pipeline (103), and then flows into the liquid oxygen tank of the heat exchange device (1) at the lower layer, and partial liquid oxygen in the first heat exchange channel (12) of the heat exchange device (1) at the uppermost layer flows downwards and flows into the liquid oxygen tank of the heat exchange device (1) at the lower layer;

and step five, repeating the step two and the step three in the lower-layer heat exchange device (1) so as to enable the liquid oxygen to be conveyed downwards until the liquid oxygen flows into the heat exchange device (1) at the lowest layer of the main cooling system, and the liquid oxygen in the heat exchange device (1) at the lowest layer flows to the bottom of the upper tower of the distillation tower (9), so that the nitrogen is liquefied, and the high-purity liquid oxygen is formed at the bottom of the upper tower of the distillation tower.

2. The main cooling method for realizing the rapid cooling of the air separation plant according to claim 1, wherein a plurality of overflow chutes are arranged in each layer of heat exchange device, a first communication pipe (110) is arranged between two adjacent overflow chutes, and after the liquid oxygen flows into the overflow chutes from the liquid oxygen tank, the liquid level communication in the overflow chutes is maintained at the same horizontal plane through the first communication pipe (110), so that the liquid oxygen uniformly flows into the first heat exchange channel below.

3. The main cooling method for realizing the rapid cooling of the air separation plant according to claim 1, characterized in that the third step comprises: s31, enabling the liquid oxygen to flow into the first heat exchange channel, enabling the liquid oxygen to uniformly distribute and flow to the first heat exchanger (122) below through the first distributor (121), enabling the liquid oxygen to partially evaporate and exchange heat through the first heat exchanger, enabling the liquid oxygen which is not evaporated to continuously flow downwards to the first distributor (121) on the next layer to be uniformly distributed again, and enabling the liquid oxygen to flow to the first heat exchanger (122) on the next layer to exchange heat until the liquid oxygen flows out from the lower part of the first heat exchange channel;

and S32, the nitrogen is divided from the flow dividing device (130) in the second heat exchange channel and then flows into the second heat exchanger (133), the nitrogen is subjected to heat exchange with the first heat exchanger through the second heat exchanger, so that the nitrogen is liquefied to form liquid nitrogen, and the liquid nitrogen flows downwards and flows out from a liquid nitrogen outlet (132) at the lower part of the second heat exchange channel.

4. The main cooling method for realizing the rapid cooling of the air separation plant according to claim 3, characterized in that the liquid level rises gradually after the liquid oxygen flows into the first heat exchange channels, when the liquid level reaches the height of the second overflow hole, the liquid oxygen flows into the second communicating pipe (124) through the second overflow hole (12 a), thereby the height of the liquid level in a plurality of first heat exchange channels can be balanced, and then the liquid oxygen flows into the first pipeline (103) through the first communicating pipe and is conveyed to the next layer.

Background

In a cryogenic air separation plant, a main cooling system is a condensing evaporator which is connected with key heat exchange equipment of an upper tower and a lower tower, and the structure and the heat transfer performance of the main cooling system have direct influence on the energy consumption, the separation efficiency and the capital investment of the air separation plant.

Along with the maximization of air separation equipment, the heat exchange efficiency and the heat exchange speed are also improved through the design of multilayer to air separation equipment's main cold system to deal with the work demand of air separation equipment high load, but current multilayer main cold system still has multiple shortcomings such as heat exchange efficiency is lower, needs to improve main cold system.

Disclosure of Invention

In view of the above problems, the present application provides a main cooling method for realizing rapid cooling of an air separation plant, so as to improve the performance of an air separation multi-layer main cooling system.

The invention provides a main cooling method for realizing rapid cooling of an air separation plant, which comprises the following steps:

firstly, conveying nitrogen from a lower tower of a distillation tower to a second heat exchange channel of each layer of heat exchange device; the liquid oxygen flows downwards from the upper layer of the distillation tower and flows into a liquid oxygen tank of the uppermost heat exchange device of the main cooling system.

And secondly, part of the liquid oxygen flows into the overflow groove below from the liquid outlet channel, and the liquid oxygen overflows from the top of the overflow groove and flows into the first heat exchange channel below after the overflow groove is filled with the liquid oxygen.

And thirdly, partially evaporating the liquid oxygen in the first heat exchange channel to exchange heat with the nitrogen in the second heat exchange channel, so that the nitrogen is liquefied to form liquid nitrogen.

And fourthly, the liquid oxygen in the liquid oxygen tank at the uppermost layer rises to the position of the first overflow hole, flows out of the first overflow hole and flows into the inflow port at the lower part through the first pipeline, so that the liquid oxygen flows into the liquid oxygen tank of the heat exchange device at the lower layer, and partial liquid oxygen in the first heat exchange channel of the heat exchange device at the uppermost layer flows downwards and flows into the liquid oxygen tank of the heat exchange device at the lower layer.

And fifthly, repeating the second step and the third step in the lower-layer heat exchange device, so that the liquid oxygen is conveyed downwards until the liquid oxygen flows into the lowest-layer heat exchange device of the main cooling system, and the liquid oxygen in the lowest-layer heat exchange device flows to the bottom of the upper tower of the distillation tower, so that the nitrogen is liquefied, and the high-purity liquid oxygen is formed at the bottom of the upper tower of the distillation tower.

Furthermore, a plurality of overflow chutes are arranged in each layer of heat exchange device, a first communication pipe is arranged between every two adjacent overflow chutes, and liquid levels in the overflow chutes are communicated and maintained on the same horizontal plane through the first communication pipe after liquid oxygen flows into the overflow chutes from the liquid oxygen chutes, so that the liquid oxygen uniformly flows into the first heat exchange channel below.

Further, the third step includes: s31, enabling the liquid oxygen to flow into the first heat exchange channel, enabling the liquid oxygen to uniformly distribute through the first distributor and flow to the first heat exchanger below, enabling the liquid oxygen to partially evaporate and exchange heat through the first heat exchanger, enabling the liquid oxygen which is not evaporated to continuously flow downwards to the first distributor on the next layer to be uniformly distributed again and then flow to the first heat exchanger on the next layer to exchange heat until the liquid oxygen flows out from the lower portion of the first heat exchange channel.

S32, the nitrogen is shunted from the shunting device in the second heat exchange channel and then flows into the second heat exchanger, and heat exchange is carried out between the nitrogen and the first heat exchanger through the second heat exchanger, so that the nitrogen is liquefied to form liquid nitrogen, and the liquid nitrogen flows downwards and flows out from a liquid nitrogen outlet at the lower part of the second heat exchange channel.

Further, liquid oxygen flows into first heat transfer passageway back liquid level and rises gradually, and when the liquid level reached the height of second overflow hole, liquid oxygen flowed into the second communicating pipe through the second overflow hole to can balance the height of liquid level in a plurality of first heat transfer passageways, then liquid oxygen flowed into first pipeline through first communicating pipe, carried to next floor.

Furthermore, in order to ensure that the main cooling method can be effectively and safely implemented, the method also comprises a multi-layer main cooling system for the air separation plant, which is arranged in the distillation tower and comprises a plurality of heat exchange devices which are sequentially arranged at intervals along the vertical direction, each heat exchange device comprises a liquid oxygen tank, a plurality of first heat exchange channels which are vertically arranged are uniformly arranged below the liquid oxygen tank at intervals, a second heat exchange channel is formed between every two adjacent first heat exchange channels, an overflow groove capable of covering the second heat exchange channel is arranged at the top of each second heat exchange channel, the top of each overflow groove is positioned on the same horizontal plane, liquid outlet channels which are in one-to-one correspondence with the overflow grooves are arranged at the bottom of the liquid oxygen tank, liquid oxygen overflowing from the overflow grooves can flow into the two adjacent first heat exchange channels, and first overflow holes are arranged on the liquid oxygen tank, and an inflow port is formed in the side wall of the distillation tower and is positioned below each heat exchange device, a first overflow hole of each heat exchange device is communicated with the inflow port below the heat exchange device through a first pipeline, and the second heat exchange channel is provided with a nitrogen inlet and a liquid nitrogen outflow port.

Further, the first heat exchange channel comprises two side walls which are arranged in parallel; the second heat exchange channel is arranged between two adjacent first heat exchange channels and shares a side wall with the two adjacent first heat exchange channels.

Further, at least one communicating pipe is arranged between every two adjacent overflow grooves.

Furthermore, the lower part of the first heat exchange channel is provided with an opening, a first distributor and a first heat exchanger are sequentially and alternately arranged in the first heat exchange channel from top to bottom, and at least two first distributors and at least two first heat exchangers are arranged.

Furthermore, a plurality of second overflow holes are formed in the side wall of the first heat exchange channel, the second overflow holes are located on the same horizontal plane of the cylinder, the second overflow holes are formed between the uppermost layer of the first distributor and the tops of the overflow grooves, and the second overflow holes are communicated with the first pipeline.

Furthermore, the plurality of second overflow holes are all collected and communicated with a third pipeline, the third pipeline is communicated with the first pipeline, and a one-way passing valve is arranged on the third pipeline.

Furthermore, the second overflow holes in the adjacent side walls of the adjacent first heat exchange channels are communicated through a second communicating pipe, and the second communicating pipe is communicated with the third pipeline.

Further, the first distributor is a porous fin or a zigzag fin horizontally arranged on two side walls of the first heat exchange channel.

Furthermore, the inside of the second heat exchange channel is sequentially communicated with a flow dividing device and a second heat exchanger from top to bottom, the flow dividing device is provided with the nitrogen inlet, and the bottom of the second heat exchange channel is provided with the liquid nitrogen outlet.

Further, the liquid nitrogen outlet ports of the plurality of second heat exchange channels are all in gathering communication with a liquid nitrogen delivery pipe arranged outside the distillation tower.

Further, the first heat exchanger is a porous fin arranged in the first heat exchange channel, the porous fin is in thermal coupling connection with the inner side wall of the first heat exchange channel, the second heat exchanger is a porous fin arranged in the second heat exchange channel, and the porous fin is in thermal coupling connection with the outer side wall of the first heat exchange channel.

Furthermore, the first heat exchanger, the second heat exchanger and the side plates on the two sides of the first heat exchange channel are all made of aluminum heat conduction materials.

According to the main cooling method for realizing rapid cooling of the air separation plant, the distillation tower comprises the plurality of heat exchange devices which are sequentially arranged at intervals along the vertical direction, so that the heat exchange rate can be increased, the heat exchange effect is improved, the overflow groove is arranged, the liquid oxygen can be uniformly distributed in the two adjacent first heat exchange channels, the liquid oxygen is ensured to be uniformly distributed in each first heat exchange channel, and the liquid oxygen can be ensured to be uniformly distributed in the first heat exchange channels through the side overflow of the overflow groove, so that the heat exchange efficiency is improved, the heat exchange effect is further improved, and the heat exchange rate of a main cooling system is improved.

In addition, at least two first distributors and first heat exchangers are sequentially and alternately arranged in the first heat exchange channel from top to bottom, so that the film distribution effect on the liquid oxygen can be improved, the heat exchange efficiency between the liquid oxygen and the first heat exchangers is further improved, and the heat exchange rate of the main cooling system is improved.

Furthermore, at least one communicating pipe is arranged between every two adjacent overflow grooves, so that the liquid level in each overflow groove can be kept level, the phenomenon that the liquid oxygen amount in part of first heat exchange channels is large and the dry evaporation phenomenon is caused by insufficient liquid oxygen amount in part of first heat exchange channels due to unequal height of the liquid level in the overflow grooves when the liquid outlet channels are uneven is avoided, and the heat exchange efficiency and the safety of a main cooling system are ensured.

Furthermore, the second overflow holes in the adjacent side walls of the two adjacent first heat exchange channels are communicated through the second communicating pipe, so that the liquid level in each first heat exchange channel can be further guaranteed to be equal in height, the phenomenon of dry evaporation in part of the first heat exchange channels is further avoided, and the safety of the main cooling system is further improved.

Drawings

Other features, objects and advantages of the present application will become more apparent upon reading of the following detailed description of non-limiting embodiments thereof, made with reference to the accompanying drawings.

Fig. 1 is a schematic overall structure diagram of a multi-layer main cooling system for an air separation plant provided by the invention.

Fig. 2 is a schematic structural diagram of a heat exchange device in a multi-layer main cooling system for an air separation plant provided by the invention.

Fig. 3 is a schematic cross-sectional structure at a-a in a multi-layer main cooling system for an air separation plant provided by the invention.

Fig. 4 is a flow chart of a main cooling method for realizing rapid cooling of an air separation plant provided by the invention.

Detailed Description

The present application will be described in further detail with reference to the following drawings and examples. It is to be understood that the specific embodiments described herein are merely illustrative of the relevant invention and not restrictive of the invention. It should be noted that, for convenience of description, only the portions related to the present invention are shown in the drawings.

It should be noted that the embodiments and features of the embodiments in the present application may be combined with each other without conflict. The present application will be described in detail below with reference to the embodiments with reference to the attached drawings.

Example one

Referring to fig. 4, the present invention further provides a main cooling method for implementing rapid cooling of an air separation plant, including the following steps: firstly, conveying nitrogen from a lower tower of a distillation tower to a second heat exchange channel 13 of each layer of heat exchange device 1; the liquid oxygen flows downwards from the upper layer of the distillation tower and flows into a liquid oxygen tank of the heat exchange device 1 at the uppermost layer of the main cooling system;

step two, part of liquid oxygen flows into an overflow groove 11 below from a plurality of liquid outlet channels 101, and the liquid oxygen overflows from the top of the overflow groove and flows into a first heat exchange channel 12 below after the overflow groove is filled with the liquid oxygen;

thirdly, partial evaporation of the liquid oxygen in the first heat exchange channel 12 is carried out heat exchange with the nitrogen in the second heat exchange channel 13, so that the nitrogen is liquefied to form liquid nitrogen;

step four, the liquid level in the uppermost layer of liquid oxygen tank rises to the position of the first overflow hole 102, the liquid oxygen flows out, and flows into the inflow port 91 at the lower part through the first pipeline 103, so that the liquid oxygen flows into the liquid oxygen tank of the lower layer of heat exchange device 1, and part of the liquid oxygen in the first heat exchange channel of the uppermost layer of heat exchange device 1 flows downwards and flows into the liquid oxygen tank of the lower layer of heat exchange device 1;

and step five, repeating the step two and the step three in the lower-layer heat exchange device 1, so that the liquid oxygen is conveyed downwards until the liquid oxygen flows into the heat exchange device 1 at the lowest layer of the main cooling system, and the liquid oxygen in the heat exchange device 1 at the lowest layer flows to the bottom of the upper tower of the distillation tower, so that the nitrogen is liquefied, and the high-purity liquid oxygen is formed at the bottom of the upper tower of the distillation tower.

Furthermore, a plurality of overflow chutes are arranged in each layer of heat exchange device, a first communication pipe 110 is arranged between two adjacent overflow chutes, and after liquid oxygen flows into the overflow chutes from the liquid oxygen chutes, the liquid levels in the overflow chutes are communicated and maintained at the same horizontal plane through the first communication pipe, so that the liquid oxygen uniformly flows into the first heat exchange channel below.

Further, the third step includes: s31, enabling the liquid oxygen to flow into the first heat exchange channel, enabling the liquid oxygen to uniformly distribute and flow to the first heat exchanger 122 below through the first distributor 121, enabling the liquid oxygen to partially evaporate and exchange heat through the first heat exchanger, enabling the liquid oxygen which is not evaporated to continuously flow downwards to the first distributor 121 on the next layer to be uniformly distributed again, and then enabling the liquid oxygen to flow to the first heat exchanger 122 on the next layer for heat exchange until the liquid oxygen flows out from the lower part of the first heat exchange channel;

and S32, dividing the nitrogen gas by the dividing device 130 in the second heat exchange channel, allowing the nitrogen gas to flow into the second heat exchanger 133, exchanging heat with the first heat exchanger through the second heat exchanger, liquefying the nitrogen gas to form liquid nitrogen, and allowing the liquid nitrogen to flow downwards and flow out from the liquid nitrogen outlet 132 at the lower part of the second heat exchange channel.

Further, liquid level rises gradually after liquid oxygen flows into first heat transfer passageway, and when the liquid level reached the height of second overflow hole, liquid oxygen flowed into second communicating pipe to can balance the height of liquid level in a plurality of first heat transfer passageways, then liquid oxygen flowed into first pipeline 103 through first communicating pipe, carried to next floor.

Referring to fig. 1, wherein the nitrogen gas of lower tower is led out through the nitrogen gas main pipe, every layer of heat transfer device all communicates to have nitrogen gas to carry to be in charge of and liquid nitrogen carries to be in charge of, nitrogen gas carries to be in charge of all with nitrogen gas and is all in charge of the intercommunication, the nitrogen gas inlet port 131 of a plurality of second heat transfer passageways of every heat transfer device 1 all carries to be in charge of with nitrogen gas and communicates, the liquid nitrogen egress opening 132 of a plurality of second heat transfer passageways of every heat transfer device 1 all carries to be in charge of with liquid nitrogen and communicates, a plurality of liquid nitrogen carry to be in charge of all with liquid nitrogen conveyer pipe 92 intercommunication.

Example two

The invention provides a multilayer main cooling system for an air separation plant, which is arranged in a distillation tower 9, and referring to fig. 1-3, as a specific embodiment, the main cooling system comprises a plurality of heat exchange devices 1 arranged at intervals in sequence along a vertical direction, the heat exchange devices 1 comprise a liquid oxygen tank 10, a plurality of first heat exchange channels 12 arranged vertically are uniformly arranged below the liquid oxygen tank 10 at intervals, a second heat exchange channel 13 is formed between two adjacent first heat exchange channels 12, an overflow groove 11 capable of covering the second heat exchange channel 13 is arranged at the top of each second heat exchange channel 13, the top of each overflow groove is positioned at the same horizontal plane, liquid outlet channels 101 corresponding to the overflow grooves 11 one by one are arranged at the bottom of the liquid oxygen tank 10, liquid oxygen overflowing from the overflow grooves 11 can flow into two adjacent first heat exchange channels 12, the liquid oxygen tank 10 is provided with a first overflow hole 102, an inflow port 91 is arranged on the side wall of the distillation tower 9 and below each heat exchange device 1, the first overflow hole 102 of each heat exchange device 1 is communicated with the inflow port 91 below the heat exchange device through a first pipeline 103, and the second heat exchange channel 13 is provided with a nitrogen inlet 131 and a liquid nitrogen outlet 132. The heat exchange device comprises a plurality of heat exchange devices, wherein the heat exchange devices are sequentially arranged in the distillation tower at intervals along the vertical direction, so that the heat exchange speed can be increased, the heat exchange effect is improved, the overflow grooves are formed, the liquid oxygen can be equalized in two adjacent first heat exchange channels, the uniform distribution of the liquid oxygen in each first heat exchange channel is ensured, the side overflow of the overflow grooves can ensure the uniform distribution of the liquid oxygen in the first heat exchange channels, the heat exchange efficiency is improved, the heat exchange effect is further improved, and the heat exchange speed of a main cooling system is improved.

Further, referring to fig. 2, as a preferred embodiment, at least one first communication pipe 11 is arranged between two adjacent overflow chutes 11, and at least one communication pipe is arranged between two adjacent overflow chutes, so that the liquid level in each overflow chute can be ensured to be even, and the phenomena of high liquid oxygen content in part of first heat exchange channels and dry evaporation in part of first heat exchange channels due to insufficient liquid oxygen content caused by unequal liquid level in the overflow chutes when the liquid outlet channel has uneven liquid outlet are avoided, thereby ensuring the heat exchange efficiency and safety of the main cooling system.

Further, referring to fig. 2 and 3, as a specific embodiment, each heat exchange device has a specific structure that: the first heat exchange channel 12 comprises two side walls which are arranged in parallel; the second heat exchange channel 13 is arranged between two adjacent first heat exchange channels 12 and shares a side wall with the two adjacent first heat exchange channels.

Further, the lower part of the first heat exchange channel 12 is provided with an opening, a first distributor 121 and a first heat exchanger 122 are alternately arranged in the first heat exchange channel 12 from top to bottom in sequence, and at least two first distributors 121 and at least two first heat exchangers 122 are arranged; through from last to setting up two at least first distributors, first heat exchanger in proper order in turn down in first heat transfer passageway to can improve the cloth membrane effect to liquid oxygen, further improve the heat exchange efficiency between liquid oxygen and the first heat exchanger, thereby improve the heat transfer rate of main cold system.

Further, a plurality of second overflow holes 12a are formed in the side wall of the first heat exchange channel 12, the plurality of second overflow holes 12a are all located on a same horizontal plane of the cylinder, the second overflow holes 12a are disposed between the uppermost layer of the first distributor 121 and the top of the overflow groove, and the plurality of second overflow holes 12a are all communicated with the first pipeline 103.

Furthermore, the second overflow holes 12a are all collected and communicated with a third pipeline 14, the third pipeline 14 is communicated with the first pipeline 103, and a one-way passing valve 15 is arranged on the third pipeline 14. The liquid oxygen in the first channel can only be allowed to flow into the third pipeline by arranging the one-way passing valve, the liquid oxygen in the first pipeline is prevented from flowing back to the first heat exchange channel, the second overflow holes in the adjacent side walls of the two adjacent first heat exchange channels are communicated through the second communicating pipe, the liquid level in each first heat exchange channel can be further guaranteed to be equal in height, the dry evaporation phenomenon in partial first heat exchange channels is further avoided, and the safety of a main cooling system is further improved.

Further, the second overflow holes 12a on the adjacent side walls of the adjacent first heat exchange channels 12 are communicated through a second communication pipe 124, and the second communication pipe is communicated with the third pipeline 14.

Further, the first distributor 121 is a porous fin or a zigzag fin horizontally disposed on both side walls of the first heat exchange channel 12.

Further, a flow dividing device 130 and a second heat exchanger 133 are sequentially arranged inside the second heat exchange channel 13 from top to bottom in a communicating manner, the flow dividing device 130 is provided with the nitrogen inlet 131, and the bottom of the second heat exchange channel 13 is provided with the liquid nitrogen outlet 132.

Further, the liquid nitrogen outflow ports 132 of the plurality of second heat exchange passages 13 are all in collective communication with a liquid nitrogen delivery pipe 92 provided outside the distillation column 9.

Further, the first heat exchanger 122 is a porous fin disposed in the first heat exchange channel 12, and the porous fin is thermally coupled to the inner sidewall of the first heat exchange channel 12, and the second heat exchanger 133 is a porous fin disposed in the second heat exchange channel 13, and the porous fin is thermally coupled to the outer sidewall of the first heat exchange channel 12.

Further, the first heat exchanger 122, the second heat exchanger 133 and the two side plates of the first heat exchange channel 12 are all made of aluminum heat conducting materials.

Preferably, the main cooling system is provided with three layers of heat exchange devices 1, referring to fig. 2, each layer of heat exchange device 1 comprises an outer shell 10, the inner part of the outer shell is arranged at intervals through aluminum clapboards 100, the first heat exchange channel and the second heat exchange channel are formed between the clapboards, wherein the aluminum clapboards are side plates of the first heat exchange channel, and the overflow grooves are aluminum groove bodies welded on two adjacent clapboards. Furthermore, for each heat exchange device 1, the sum of the flow rates of the liquid outlet channels 101 is Q1, wherein Q1 is the flow rate of the liquid oxygen when the liquid oxygen tank is full of liquid oxygen, the sum of the flow rates of the first heat exchange channels 12 is Q2, the flow rate of the nitrogen gas input into the second heat exchange channels 13 is Q3 in units of L/S, wherein 1.5Q 2 is not less than Q1 and not less than 1.2Q 2, by this limiting way, the membrane distribution effect in the first heat exchange channels of each heat exchange device 1 can be ensured, the heat exchange efficiency can be ensured, the redundant liquid oxygen can flow into the heat exchange device below through the first overflow holes in time, the next heat exchange device can be ensured to have enough liquid oxygen, the utilization rate of the liquid oxygen is improved, and Q3 is Q2 (μ 1 μ 2S 1)^1/2*&Wherein μ 1 is the heat exchange coefficient of the first heat exchanger, μ 2 is the heat exchange coefficient of the second heat exchanger, and S1 is the sum of the contact areas of the first heat exchange channel and the second heat exchange channel, and the unit is m²，&In order to adjust the coefficient, the value range is 0.375-5.643, the flow of the nitrogen introduced into each heat exchange device is calculated by the formula, the nitrogen air inflow of each heat exchange device can be realized, and the nitrogen and the liquid oxygen can be ensured to be fully liquefied into the liquid oxygen through heat exchange.

EXAMPLE III

In order to verify the technical effect of the technical solution of the present application, the following two tests are performed in this embodiment for comparison.

Test one: the cooling is carried out during air separation by adopting the traditional technology, namely, a heat exchanger and a separation tower are tightly combined in the low-temperature separation process, and all refrigeration energy is provided by an air compressor at the inlet of the device.

And (2) test II: by adopting the technical scheme, the air separation equipment is rapidly cooled.

Through comparison of the first test and the second test, the technical scheme of the application is adopted to rapidly cool the air separation equipment to achieve the same temperature, the speed of the application is improved by 12.4-18.5% compared with the traditional mode, and the energy consumption is reduced by 5.4-10.8%.

The above description is only a preferred embodiment of the application and is illustrative of the principles of the technology employed. It will be appreciated by a person skilled in the art that the scope of the invention as referred to in the present application is not limited to the embodiments with a specific combination of the above-mentioned features, but also covers other embodiments with any combination of the above-mentioned features or their equivalents without departing from the inventive concept. For example, the above features may be replaced with (but not limited to) features having similar functions disclosed in the present application.