CN201297492Y - A recovery device of boil-off gas from a carbon dioxide storage tank - Google Patents
A recovery device of boil-off gas from a carbon dioxide storage tank Download PDFInfo
- Publication number
- CN201297492Y CN201297492Y CNU2008202377229U CN200820237722U CN201297492Y CN 201297492 Y CN201297492 Y CN 201297492Y CN U2008202377229 U CNU2008202377229 U CN U2008202377229U CN 200820237722 U CN200820237722 U CN 200820237722U CN 201297492 Y CN201297492 Y CN 201297492Y
- Authority
- CN
- China
- Prior art keywords
- gas
- carbon dioxide
- storage tank
- boil
- recovery device
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及工业级液体二氧化碳气体回收装置,特别涉及工业级液体二氧化碳气体在储罐中蒸发的气体回收的装置。The utility model relates to an industrial-grade liquid carbon dioxide gas recovery device, in particular to a gas recovery device for industrial-grade liquid carbon dioxide gas evaporated in a storage tank.
技术背景 technical background
二氧化碳生产、储运过程中,由于其自身物理特性,不能如氧、氮、氩等超低温低压储运,全气态储运更是成本效率极差。而采用中压(2.0~2.5MPa)低温(—20℃~—35℃)间储运。再储运过程中,液体二氧化碳蒸发,为保证容器压力既不能超压,又要保持较低温度,只能对蒸发气体一排了之。In the process of production, storage and transportation of carbon dioxide, due to its own physical characteristics, it cannot be stored and transported at ultra-low temperature and low pressure such as oxygen, nitrogen, and argon, and the storage and transportation in full gaseous state is extremely cost-effective. And use medium pressure (2.0 ~ 2.5MPa) low temperature (-20 ℃ ~ -35 ℃) storage and transportation. During the storage and transportation process, the liquid carbon dioxide evaporates. In order to ensure that the pressure of the container can neither exceed the pressure nor keep the temperature low, the evaporated gas can only be discharged.
上述情形中通常做法为:The usual practice in the above situation is:
1.利用部分冷量后排入大气,浪费较大。1. Use part of the cold energy and discharge it into the atmosphere, which is a big waste.
2.在罐区增加一小型冷冻系统,能有效解决问题,但过程复杂投入较大。2. Adding a small refrigeration system in the tank area can effectively solve the problem, but the process is complicated and requires a lot of investment.
发明内容 Contents of the invention
本实用新型为克服上述缺点,利用原生产装置,提供一种结构简单紧凑,对二氧化碳储罐蒸发气体回收利用的装置。In order to overcome the above disadvantages, the utility model utilizes the original production device to provide a device with simple and compact structure for recycling and utilizing the evaporated gas of the carbon dioxide storage tank.
本实用新型的技术方案是:一种二氧化碳储罐气回收装置,包括储罐,储罐内液态二氧化碳蒸发后,变为气态二氧化碳,由储罐上的蒸发气体阀门控制由蒸发气体管道排出,排放压力为1.8~2.0MPa,通过减压阀减压至0.05~0.1MPa,蒸发气体排放管路和原料管路之间增加一条连通管路,蒸发气体和原料气体混合后,原料气温度下降后,有更多水份析出,进入过滤阀组过滤,由二氧化碳压缩系统进行压缩,然后作为产品进行充装。The technical scheme of the utility model is: a carbon dioxide storage tank gas recovery device, including a storage tank, after the liquid carbon dioxide in the storage tank evaporates, it becomes gaseous carbon dioxide, which is controlled by the evaporated gas valve on the storage tank and discharged from the evaporated gas pipeline. The pressure is 1.8-2.0MPa, and the pressure is reduced to 0.05-0.1MPa through the pressure reducing valve. A connecting pipeline is added between the evaporating gas discharge pipeline and the raw material pipeline. After the evaporating gas and raw material gas are mixed, the temperature of the raw material gas drops. More water is precipitated, filtered into the filter valve group, compressed by the carbon dioxide compression system, and then filled as a product.
其中所述的减压阀可以将二氧化碳储罐蒸发气体减压,使其压力由储罐内较高压,降为略高于二氧化碳原料气压力,将蒸发气直接引入原料管内,与原料气混合。The pressure reducing valve mentioned therein can reduce the pressure of the evaporated gas of the carbon dioxide storage tank so that its pressure is lowered from a relatively high pressure in the storage tank to slightly higher than the pressure of the carbon dioxide raw material gas, and the evaporated gas is directly introduced into the raw material pipe to be mixed with the raw material gas.
本实用新型设备改装简单,投入小,充分回收利用了蒸发气体,二氧化碳蒸发气体纯度较高,与原料二氧化碳混合后,使原料气纯度提高,更利于气体液化,降低原料气含水量,较大提高生产效率。The equipment of the utility model is simple to refit, requires less investment, fully recycles and utilizes the evaporated gas, and the purity of the evaporated gas of carbon dioxide is high. After mixing with raw material carbon dioxide, the purity of the raw material gas is improved, which is more conducive to gas liquefaction, reduces the water content of the raw material gas, and greatly improves Productivity.
附图说明 Description of drawings
图1为本实用新型装置结构图;Fig. 1 is the structural diagram of the utility model device;
其中:1、储罐,2、蒸发气体阀门,3、蒸发气体排放管,4、减压阀,5、排空阀,6、流量控制阀,7、连通管路,8、原料气体管路,9、过滤器阀组,10、二氧化碳压缩系统。Among them: 1. Storage tank, 2. Evaporated gas valve, 3. Evaporated gas discharge pipe, 4. Pressure reducing valve, 5. Empty valve, 6. Flow control valve, 7. Connecting pipeline, 8. Raw material gas pipeline , 9, filter valve group, 10, carbon dioxide compression system.
具体设施方法specific facility method
如图1所示,一种二氧化碳储罐气回收装置,包括储罐1,储罐1上设有蒸发气体排放管3,排放流量由蒸发气体阀门2控制,蒸发气体排放管3接通连通管路7与原料气体管路8连通,蒸发气体排放管3在连通管路之前设有减压阀4,用以将蒸发气体的压力由1.8~2.0MPa,减压至0.05~0.1Mpa,使之与原料气体的压力相当,蒸发气体排放管3上端还设有排空阀5用以将多余蒸气排空,连通管路7上设有流量控制阀6用以控制通过连通管路的二氧化碳蒸发气体的流量,二氧化碳蒸发气体与原料气体混合后通过过滤阀组9过滤其中的水分和杂质然后进入二氧化碳压缩系统10进行压缩,然后作为产品进行充装。As shown in Figure 1, a carbon dioxide storage tank gas recovery device, including a
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202377229U CN201297492Y (en) | 2008-12-31 | 2008-12-31 | A recovery device of boil-off gas from a carbon dioxide storage tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202377229U CN201297492Y (en) | 2008-12-31 | 2008-12-31 | A recovery device of boil-off gas from a carbon dioxide storage tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201297492Y true CN201297492Y (en) | 2009-08-26 |
Family
ID=41043472
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008202377229U Expired - Fee Related CN201297492Y (en) | 2008-12-31 | 2008-12-31 | A recovery device of boil-off gas from a carbon dioxide storage tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201297492Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102269327A (en) * | 2011-07-28 | 2011-12-07 | 中国寰球工程公司 | Recovery system and recovery method for vapor in storage tank |
| CN104428577A (en) * | 2012-07-13 | 2015-03-18 | 乔治洛德方法研究和开发液化空气有限公司 | Method and apparatus for vaporising carbon dioxide-rich liquid |
| CN104662354A (en) * | 2012-07-03 | 2015-05-27 | 里恩格特恩纳有限公司 | Tank |
| CN105040318A (en) * | 2015-07-27 | 2015-11-11 | 华东理工大学 | Device for continuous waterless dyeing of spindles by adoption of high-pressure supercritical fluid technology |
| CN108613011A (en) * | 2018-05-17 | 2018-10-02 | 安庆凯美特气体有限公司 | The utilization method of liquid CO 2 tank top gas and utilize device |
-
2008
- 2008-12-31 CN CNU2008202377229U patent/CN201297492Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102269327A (en) * | 2011-07-28 | 2011-12-07 | 中国寰球工程公司 | Recovery system and recovery method for vapor in storage tank |
| CN104662354A (en) * | 2012-07-03 | 2015-05-27 | 里恩格特恩纳有限公司 | Tank |
| CN104428577A (en) * | 2012-07-13 | 2015-03-18 | 乔治洛德方法研究和开发液化空气有限公司 | Method and apparatus for vaporising carbon dioxide-rich liquid |
| CN104428577B (en) * | 2012-07-13 | 2016-04-06 | 乔治洛德方法研究和开发液化空气有限公司 | For evaporating the method and apparatus of rich carbonated liquid |
| CN105040318A (en) * | 2015-07-27 | 2015-11-11 | 华东理工大学 | Device for continuous waterless dyeing of spindles by adoption of high-pressure supercritical fluid technology |
| CN105040318B (en) * | 2015-07-27 | 2017-05-17 | 华东理工大学 | Device for continuous waterless dyeing of spindles by adoption of high-pressure supercritical fluid technology |
| CN108613011A (en) * | 2018-05-17 | 2018-10-02 | 安庆凯美特气体有限公司 | The utilization method of liquid CO 2 tank top gas and utilize device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101818088B (en) | Efficient continuous preparation method and device for natural gas hydrate | |
| CN201297492Y (en) | A recovery device of boil-off gas from a carbon dioxide storage tank | |
| CN104560201B (en) | The production technology and system and ammonia synthesis process and system of high-purity hydrogen | |
| CN108355461A (en) | Sulfur hexafluoride and nitrogen mixed gas purification separation purifying plant and its reclaiming clean purify sulfur hexafluoride method | |
| CN110686464A (en) | Method and device for recovering helium in flash steam of liquefied natural gas | |
| CN103274359A (en) | Method and device for recycling hydrogen from synthesis ammonia released air and preparing LNG (liquefied natural gas) with membrane separation and cryogenic integration technology | |
| CN104140085B (en) | The apparatus and method of water and carbon dioxide in a kind of deep removal nitrous oxide | |
| CN202756905U (en) | Evaporated-gas recovery device for carbon dioxide storage tank | |
| CN111256431B (en) | A mixed refrigerant biogas pressurized liquefaction system and its working method | |
| CN201692683U (en) | Device for recovering gaseous methane from membrane hydrogen extraction tail gas | |
| CN102030314A (en) | Oxygen generator | |
| CN222434400U (en) | Helium extraction system combined with natural gas denitrification liquefaction process | |
| CN209052806U (en) | A kind of single crystal growing furnace argon recovery systems | |
| CN103539603A (en) | Method for preparing liquefied methane by using synthesis ammonia vent gas and purge gas | |
| CN104194853B (en) | The device of the coalbed methane containing oxygen synthesis LNG of a kind of methane content 15-40% and technique | |
| CN207123117U (en) | A kind of new double tower nitrogen device for making | |
| CN206113508U (en) | Air separation device goes out tower nitrogen gas recovery unit | |
| CN107754558B (en) | A kind of polyethylene glycol dimethyl ether desulfurization and concentration method | |
| CN203612972U (en) | Device for recycling ammonia from waste gas in ammonia synthetizing system | |
| CN105038881B (en) | Method for continuously separating biogas by pressure swing adsorption | |
| CN100358609C (en) | Coalbed gas condensation method | |
| CN103253666B (en) | Method and complete set of equipment for reducing oxygen content in gasification process of CO2 gas of brewery | |
| CN207498327U (en) | A kind of equipment for being pressurized film purifying biogas and preparing natural gas | |
| CN104944372A (en) | Device and method for separating and recovering nitrogen, hydrogen and carbon dioxide in carbon dioxide exhaust air | |
| CN106753631A (en) | The process of reinforcing desorption type methane purification and recovery carbon dioxide |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: 215000 Jiangsu city in Suzhou Province town of Xiangcheng District Wong Tai Pan Yang Industrial Park min Road Patentee after: Suzhou Jinhong Gas Co., Ltd. Address before: Sudai road in Suzhou City, Jiangsu province 215131 No. 78 Patentee before: Suzhou Jinhong Gas Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090826 Termination date: 20151231 |