CN208804958U - A kind of integrated form carbon dioxide purification liquefying plant small in size - Google Patents

A kind of integrated form carbon dioxide purification liquefying plant small in size Download PDF

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Publication number
CN208804958U
CN208804958U CN201821642016.2U CN201821642016U CN208804958U CN 208804958 U CN208804958 U CN 208804958U CN 201821642016 U CN201821642016 U CN 201821642016U CN 208804958 U CN208804958 U CN 208804958U
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China
Prior art keywords
connecting tube
bolted
carbon dioxide
connection
tube
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CN201821642016.2U
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Chinese (zh)
Inventor
陈焕忠
石唯
徐琨璘
曾杨文
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Huizhou huadatong Gas Manufacturing Co., Ltd
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Huizhou Huadatong Petrochemical Co Ltd
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Abstract

The utility model discloses a kind of integrated form carbon dioxide purification liquefying plants small in size, including substrate, the bottom of the substrate has been bolted to connection supporting leg, and connecting rod there are two being bolted to connection at the top of substrate, the base plate bottom has been bolted to connection cooling cylinder at a side position of supporting leg, the side of the cooling cylinder is equipped with cooling water outlet and cooling water inlet, the other side has been bolted to connection water pump, the cooling water outlet is located at the lower section of cooling water inlet, the bottom of the water pump is equipped with circulation inlet tube, and water pump is equipped with circulation outlet tube relative to the side of cooling cylinder, the utility model is provided with coil pipe, ammonia separator, liquefier and subcooler, it is low to solve space utilization rate, the problem of underusing upper space, reduce the volume of device, improve space Utilization rate allows device installation without being mounted on a plane, makes full use of the upper space of device.

Description

A kind of integrated form carbon dioxide purification liquefying plant small in size
Technical field
The utility model belongs to carbon dioxide purification liquefying plant technical field, and in particular to a kind of integrated form small in size Carbon dioxide purification liquefying plant.
Background technique
It is a kind of colorless and odorless, non-flammable gas under carbon dioxide room temperature, density ratio air is big, is slightly soluble in water, is empty One of main component in gas is common greenhouse gases, a kind of gaseous compound.
The volume of existing carbon dioxide purification liquefying plant is more huge, reduces space utilization rate, and mounting means is One horizontal layout, underuses upper space, is not provided with the device convenient for coolant liquid to be recycled, needs wave Take a large amount of coolant liquids to be cooled down, use cost is larger, waste of resource.
Utility model content
The purpose of this utility model is to provide a kind of integrated form carbon dioxide purification liquefying plants small in size, to solve Reduction space utilization rate mentioned above in the background art underuses upper space and needs to waste a large amount of coolant liquids progress The problem of cooling, waste of resource.
To achieve the above object, the utility model provides the following technical solutions: a kind of integrated form carbon dioxide small in size Purifying and liquefying device, including substrate, the bottom of the substrate has been bolted to connection supporting leg, and passes through at the top of substrate Bolt is fixedly connected there are two connecting rod, and the base plate bottom has been bolted to connection cold at a side position of supporting leg Solidifying case, the side of the cooling cylinder are equipped with cooling water outlet and cooling water inlet, and the other side has been bolted to connection water Pump, the cooling water outlet are located at the lower section of cooling water inlet, and the bottom of the water pump is equipped with circulation inlet tube, and water pump phase Circulation outlet tube is equipped with for the side of cooling cylinder, the inside of the cooling cylinder is equipped with circulating box, two connecting rods it Between purifying column is installed, the inside of the purifying column is equipped with heating tube, and the side of the purifying column is equipped with switch, and purifies The bottom of tower is equipped with liquid carbon outlet pipe, and the side of the liquid carbon outlet pipe is equipped with the 7th connecting tube, and the top of the purifying column is logical It crosses bolt and is fixedly connected with ammonia separator, the side of the ammonia separator is equipped with third connecting tube, and the other side is equipped with 5th connecting tube, the purifying column have been bolted to connection liquefier adjacent to the side of switch, and the other side was equipped with Cooler is equipped with third connecting tube at the top of the liquefier, and the bottom of liquefier is equipped with the first connecting tube, the liquefaction The inside of device is equipped with coil pipe, the 4th connecting tube is equipped at the top of the coil pipe, and the bottom of coil pipe is equipped with the second connection It manages, the 5th connecting tube is installed at the top of the subcooler, and the bottom of subcooler is equipped with the 6th connecting tube, the subcooler Side relative to purifying column is equipped with the outlet of liquid carbon, and the water pump and heating tube are electrically connected with switch.
Preferably, the bottom of the supporting leg is provided with Slippery proof foot pad.
Preferably, the 7th connecting tube is fixedly connected relative to one end of liquid carbon outlet pipe with subcooler.
Preferably, the side of the liquid carbon outlet pipe is provided with valve.
Preferably, it is offered at the top of the ammonia separator convenient for the aperture of ammonia is added.
Compared with prior art, the utility model has the beneficial effects that
(1) the utility model is provided with coil pipe, ammonia separator, liquefier and subcooler, the atmospheric carbon dioxide of generation It is liquefied by coil pipe, ammonia separator stores liquefied ammonia, and the liquefied ammonia in liquefier cools down to coil pipe, subcooler Cool down to liquid CO 2, solve that space utilization rate is low, and mounting means is a horizontal layout, underuses The problem of upper space, reduces the volume of device, improves space utilization rate, allows device installation without being mounted on a plane, Make full use of the upper space of device.
(2) the utility model is provided with the first connecting tube, the 6th connecting tube, circulating box, cooling cylinder, water pump and recycles liquid Pipe, the liquefied ammonia after use are flowed back in circulating box by the first connecting tube and the 6th connecting tube, and the water body in cooling cylinder is to liquefied ammonia Cool down, water pump extracts the liquefied ammonia in circulating box and drained back into ammonia separator by recycling outlet tube, solves and needs wave Take a large amount of coolant liquids to be cooled down, the problem of use cost is larger, waste of resource, device is allowed to be convenient for carrying out coolant liquid into circulation making With being cooled down woth no need to waste a large amount of coolant liquids, use cost is larger, waste of resource.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model;
Fig. 2 is the internal structure chart of the utility model;
Fig. 3 is the enlarged drawing of the utility model a-quadrant;
In figure: 1- cooling cylinder;2- cooling water outlet;The cooling water inlet 3-;4- supporting leg;5- liquid carbon outlet pipe;6- connecting rod;7- Purifying column;The first connecting tube of 8-;The second connecting tube of 9-;10- liquefier;11- third connecting tube;The 4th connecting tube of 12-;13- ammonia Gas separating device;The 5th connecting tube of 14-;The outlet of 15- liquid carbon;16- subcooler;17- switch;The 6th connecting tube of 18-;19- the 7th connects Adapter tube;20- substrate;21- recycles outlet tube;22- recycles inlet tube;23- water pump;24- circulating box;25- coil pipe;26- heating tube.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work Every other embodiment obtained, fall within the protection scope of the utility model.
It please refers to shown in Fig. 1-Fig. 3, the utility model provides the following technical solutions: a kind of integrated form titanium dioxide small in size Carbon purifying and liquefying device, including substrate 20, the bottom of substrate 20 have been bolted to connection supporting leg 4, and the top of substrate 20 Portion is bolted to connection there are two connecting rod 6,20 bottom of substrate company of being bolted at a side position of supporting leg 4 It is connected to cooling cylinder 1, the side of cooling cylinder 1 is equipped with cooling water outlet 2 and cooling water inlet 3, when user needs use device When, it adds raw materials into purifying column 7, heating tube 26 is started by switch 17, heating tube 26 carries out heating purification to raw material, generates Atmospheric carbon dioxide by the 4th connecting tube 12 enter coil pipe 25, liquefied ammonia from ammonia separator 13 enter third connecting tube 11 In, to reach in liquefier 10, cool down to the atmospheric carbon dioxide in coil pipe 25, makes liquefied carbon dioxide by the Two connecting tubes 9 enter in purifying column 7, and liquid CO 2 is flowed in the 7th connecting tube 19 by liquid carbon outlet pipe 5, hence into In subcooler 16, liquefied ammonia enters in the 5th connecting tube 14 from ammonia separator 13, so that subcooler 16 is flowed into, to liquid titanium dioxide Carbon cools down, and by 15 discharge of liquid carbon outlet, the other side has been bolted to connection the liquid CO 2 after being cooled down Water pump 23, water pump 23 use 50CQ-25 water pump, voltage 380V, revolving speed 2900r/min, flow 14.4m3/h, cooling water Outlet 2 is located at the lower section of cooling water inlet 3, and the bottom of water pump 23 is equipped with circulation inlet tube 22, and water pump 23 is relative to condensation The side of case 1 is equipped with circulation outlet tube 21, and the inside of cooling cylinder 1 is equipped with circulating box 24, is equipped with and mentions between two connecting rods 6 Pure tower 7, the inside of purifying column 7 are equipped with heating tube 26, and the side of purifying column 7 is equipped with switch 17, and the bottom peace of purifying column 7 Equipped with liquid carbon outlet pipe 5, the side of liquid carbon outlet pipe 5 is equipped with the 7th connecting tube 19, and the liquefied ammonia after use passes through 8 He of the first connecting tube 6th connecting tube 18 flows back in circulating box 24, and the lower water body of temperature is added by cooling water inlet 3 into cooling cylinder 1, Water body cools down to liquefied ammonia, and the raised water body of temperature is discharged from cooling water outlet 2, starts water pump 23, water pump by switch 17 23 extract the liquefied ammonia in circulating box 24, are drained back into ammonia separator 13 by recycling outlet tube 21, complete the circulation of liquefied ammonia It uses, the top of purifying column 7 has been bolted to connection ammonia separator 13, and the side of ammonia separator 13 is equipped with third Connecting tube 11, the other side are equipped with the 5th connecting tube 14, and purifying column 7 has been bolted to connection adjacent to the side of switch 17 Liquefier 10, the other side are equipped with subcooler 16, and the top of liquefier 10 is equipped with third connecting tube 11, and the bottom of liquefier 10 Portion is equipped with the first connecting tube 8, and the inside of liquefier 10 is equipped with coil pipe 25, and the top of coil pipe 25 is equipped with the 4th connecting tube 12, and the bottom of coil pipe 25 is equipped with the second connecting tube 9, the top of subcooler 16 is equipped with the 5th connecting tube 14, and subcooler 16 bottom is equipped with the 6th connecting tube 18, and subcooler 16 is equipped with liquid carbon outlet 15, water pump 23 relative to the side of purifying column 7 It is electrically connected with switch 17 with heating tube 26.
In order to increase the skid resistance of supporting leg 4, in the present embodiment, it is preferred that the bottom of supporting leg 4 is provided with non-slip feet Pad.
In order to which liquid carbon enters subcooler 16, in the present embodiment, it is preferred that the 7th connecting tube 19 is relative to liquid carbon outlet pipe 5 One end is fixedly connected with subcooler 16.
For the ease of controlling the flowing of liquid, in the present embodiment, it is preferred that the side of liquid carbon outlet pipe 5 is provided with valve.
For the ease of raw material is added, in the present embodiment, it is preferred that offered at the top of ammonia separator 13 convenient for ammonia is added Aperture.
The working principle and process for using of the utility model: when user needs use device, purification is added raw materials into In tower 7, heating tube 26 is started by switch 17, heating tube 26 carries out heating purification to raw material, and the atmospheric carbon dioxide of generation is logical It crosses the 4th connecting tube 12 and enters coil pipe 25, liquefied ammonia enters in third connecting tube 11 from ammonia separator 13, to reach liquefier In 10, cool down to the atmospheric carbon dioxide in coil pipe 25, liquefied carbon dioxide is made to enter purification by the second connecting tube 9 In tower 7, liquid CO 2 is flowed in the 7th connecting tube 19 by liquid carbon outlet pipe 5, hence into subcooler 16, liquefied ammonia from Ammonia separator 13 enters in the 5th connecting tube 14, to flow into subcooler 16, cools down to liquid CO 2, is cooled down Liquid CO 2 afterwards completes the proposition of carbon dioxide, the liquefied ammonia after use connects by first by 15 discharge of liquid carbon outlet Adapter tube 8 and the 6th connecting tube 18 flow back in circulating box 24, and the lower water body of temperature is added by cooling water inlet 3 to condensation In case 1, water body cools down to liquefied ammonia, and the raised water body of temperature is discharged from cooling water outlet 2, starts water pump by switch 17 23, water pump 23 extracts the liquefied ammonia in circulating box 24, is drained back into ammonia separator 13 by recycling outlet tube 21, completes liquefied ammonia Recycling.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art, It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.

Claims (5)

1. a kind of integrated form carbon dioxide purification liquefying plant small in size, including substrate (20), it is characterised in that: the substrate (20) bottom has been bolted to connection supporting leg (4), and there are two being bolted to connection at the top of substrate (20) Connecting rod (6), substrate (20) bottom have been bolted to connection cooling cylinder (1) at a side position of supporting leg (4), The side of the cooling cylinder (1) is equipped with cooling water outlet (2) and cooling water inlet (3), and the other side is bolted to connection Have water pump (23), the cooling water outlet (2) is located at the lower section of cooling water inlet (3), and the bottom of the water pump (23) is equipped with It recycles inlet tube (22), and water pump (23) is equipped with circulation outlet tube (21), the cooling cylinder relative to the side of cooling cylinder (1) (1) inside is equipped with circulating box (24), is equipped with purifying column (7) between two connecting rods (6), the purifying column (7) Inside is equipped with heating tube (26), and the side of the purifying column (7) is equipped with switch (17), and the bottom installation of purifying column (7) There is liquid carbon outlet pipe (5), the side of the liquid carbon outlet pipe (5) is equipped with the 7th connecting tube (19), and the top of the purifying column (7) is logical Bolt to be crossed to be fixedly connected with ammonia separator (13), the side of the ammonia separator (13) is equipped with third connecting tube (11), The other side is equipped with the 5th connecting tube (14), and the purifying column (7) is bolted to connection adjacent to the side of switch (17) Having liquefier (10), the other side is equipped with subcooler (16), third connecting tube (11) are installed at the top of the liquefier (10), And the bottom of liquefier (10) is equipped with the first connecting tube (8), the inside of the liquefier (10) is equipped with coil pipe (25), described 4th connecting tube (12) is installed, and the bottom of coil pipe (25) is equipped with the second connecting tube (9), the mistake at the top of coil pipe (25) 5th connecting tube (14) is installed, and the bottom of subcooler (16) is equipped with the 6th connecting tube (18), institute at the top of cooler (16) It states subcooler (16) and liquid carbon outlet (15), the water pump (23) and heating tube (26) is installed relative to the side of purifying column (7) It is electrically connected with switch (17).
2. one kind according to claim 1 integrated form carbon dioxide purification liquefying plant small in size, it is characterised in that: institute The bottom for stating supporting leg (4) is provided with Slippery proof foot pad.
3. one kind according to claim 1 integrated form carbon dioxide purification liquefying plant small in size, it is characterised in that: institute One end that the 7th connecting tube (19) is stated relative to liquid carbon outlet pipe (5) is fixedly connected with subcooler (16).
4. one kind according to claim 1 integrated form carbon dioxide purification liquefying plant small in size, it is characterised in that: institute The side for stating liquid carbon outlet pipe (5) is provided with valve.
5. one kind according to claim 1 integrated form carbon dioxide purification liquefying plant small in size, it is characterised in that: institute It states and is offered at the top of ammonia separator (13) convenient for the aperture of ammonia is added.
CN201821642016.2U 2018-10-10 2018-10-10 A kind of integrated form carbon dioxide purification liquefying plant small in size Active CN208804958U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821642016.2U CN208804958U (en) 2018-10-10 2018-10-10 A kind of integrated form carbon dioxide purification liquefying plant small in size

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821642016.2U CN208804958U (en) 2018-10-10 2018-10-10 A kind of integrated form carbon dioxide purification liquefying plant small in size

Publications (1)

Publication Number Publication Date
CN208804958U true CN208804958U (en) 2019-04-30

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821642016.2U Active CN208804958U (en) 2018-10-10 2018-10-10 A kind of integrated form carbon dioxide purification liquefying plant small in size

Country Status (1)

Country Link
CN (1) CN208804958U (en)

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GR01 Patent grant
GR01 Patent grant
CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 510670 No.1, Youcheng West Road, Aotou, Dayawan, Huizhou City, Guangdong Province

Patentee after: Huizhou huadatong Gas Manufacturing Co., Ltd

Address before: 516082 No. 1, West Aotou Youcheng Road, Daya Bay, Huizhou City, Guangdong Province

Patentee before: HUIZHOU HUADATONG PETROCHEMICAL Co.,Ltd.

CB03 Change of inventor or designer information
CB03 Change of inventor or designer information

Inventor after: Chen Huanzhong

Inventor after: Shi Wei

Inventor after: Xu Kunlin

Inventor after: Zeng Yangwen

Inventor before: Chen Huanzhong

Inventor before: Shi Wei

Inventor before: Xu Kunlin

Inventor before: Zeng Yangwen