CN204147734U - The empty separating and purifying device of a kind of runner - Google Patents
The empty separating and purifying device of a kind of runner Download PDFInfo
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- CN204147734U CN204147734U CN201420478812.2U CN201420478812U CN204147734U CN 204147734 U CN204147734 U CN 204147734U CN 201420478812 U CN201420478812 U CN 201420478812U CN 204147734 U CN204147734 U CN 204147734U
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- 238000011069 regeneration method Methods 0.000 claims abstract description 58
- 230000008929 regeneration Effects 0.000 claims abstract description 54
- 238000000926 separation method Methods 0.000 claims abstract description 36
- 238000000746 purification Methods 0.000 claims abstract description 29
- 238000001179 sorption measurement Methods 0.000 claims abstract description 26
- 230000001172 regenerating effect Effects 0.000 claims abstract description 23
- 238000001816 cooling Methods 0.000 claims abstract description 18
- 238000004887 air purification Methods 0.000 claims abstract description 17
- 238000010438 heat treatment Methods 0.000 claims abstract description 16
- 239000003463 adsorbent Substances 0.000 claims abstract description 14
- 239000002808 molecular sieve Substances 0.000 claims description 12
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 12
- 239000010410 layer Substances 0.000 claims description 11
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000002356 single layer Substances 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 17
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 229910002092 carbon dioxide Inorganic materials 0.000 description 9
- 239000001569 carbon dioxide Substances 0.000 description 9
- 239000012535 impurity Substances 0.000 description 7
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
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- 238000004519 manufacturing process Methods 0.000 description 3
- 229910052786 argon Inorganic materials 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- -1 moisture Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
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- 238000004886 process control Methods 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
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- Separation Of Gases By Adsorption (AREA)
Abstract
一种转轮空分纯化装置,该装置包括依次连接的空气过滤器、空气压缩机、空气预冷塔、空气纯化装置和空气增压机,空气纯化装置包括相间隔的空气管道、再生热风管道和再生冷风管道,还包括转轮型吸附器以及与转轮型吸附器连接并控制其旋转的转动电机,空气管道、再生热风管道和再生冷风管道将转轮型吸附器分别分为吸附区、再生加热区和再生冷却区,吸附区、再生加热区和再生冷却区中均匀布置有多个仓格板,仓格板间装有吸附剂;本实用新型还提供了空分纯化的方法,通过优化空分纯化系统的工艺流程从而简化其程控系统来降低故障发生率,以保持吸附剂优良的吸附性能,提高空分纯化系统工作效率,延长空分设备寿命。
A rotary air separation and purification device, the device includes an air filter, an air compressor, an air precooling tower, an air purification device and an air booster connected in sequence, and the air purification device includes spaced air pipes, regenerative hot air pipes and the regenerative cold air pipeline, which also includes a rotary adsorber and a rotating motor connected with the rotary adsorber and controlling its rotation. The regeneration heating zone and the regeneration cooling zone, the adsorption zone, the regeneration heating zone and the regeneration cooling zone are evenly arranged with a plurality of compartment grids, and adsorbents are installed between the compartment grids; the utility model also provides an air separation and purification method, through Optimize the process flow of the air separation purification system to simplify its program control system to reduce the incidence of failures, to maintain the excellent adsorption performance of the adsorbent, improve the working efficiency of the air separation purification system, and prolong the life of the air separation equipment.
Description
技术领域technical field
本实用新型属于空气分离技术领域,具体涉及一种转轮空分纯化装置。The utility model belongs to the technical field of air separation, in particular to a rotary air separation and purification device.
背景技术Background technique
空气分离系统在煤化工、洁净煤发电等工业领域中占有至关重要的地位。现代大型空分工艺所应用的原理是利用低温下空气中各组分沸点的不同,通过一系列的工艺过程将空气液化,利用精馏塔精馏工艺分离各组分,并得到高纯度气体产品。为了避免空气中水分和二氧化碳等物质在进入空气分离设备低温区后形成冰和干冰从而阻塞换热器通道和塔板上的小孔,在气体进入分馏塔之前,先通入纯化系统。空分纯化系统,是一种去除空气中水分、二氧化碳及碳氢化合物等杂质的装置,从而提升空分过程稳定性和效率,防止进塔空气中的水分和二氧化碳影响设备的正常运转。空气纯化装置是空气纯化系统中的核心设备,其空气处理规模与效果直接影响到整个空分系统的规模、运行的稳定性和经济性。Air separation system occupies a vital position in industrial fields such as coal chemical industry and clean coal power generation. The principle applied in the modern large-scale air separation process is to use the difference in the boiling point of each component in the air at low temperature to liquefy the air through a series of processes, and use the distillation column to separate the components and obtain high-purity gas products . In order to prevent substances such as moisture and carbon dioxide in the air from forming ice and dry ice after entering the low-temperature zone of the air separation equipment, thereby blocking the heat exchanger channels and small holes on the tray plate, the gas is first passed into the purification system before entering the fractionation tower. The air separation purification system is a device that removes impurities such as moisture, carbon dioxide and hydrocarbons in the air, thereby improving the stability and efficiency of the air separation process and preventing the moisture and carbon dioxide in the air entering the tower from affecting the normal operation of the equipment. The air purification unit is the core equipment in the air purification system, and its air treatment scale and effect directly affect the scale, operation stability and economy of the entire air separation system.
现有的空分设备纯化系统一般由两台切换使用的吸附器(即空气纯化装置)、再生加热设备以及阀门、管路、仪电控等组成。正常运行时一台吸附器吸附,另一台则进行再生。待一台吸附饱和后,另一台再生好的吸附器便投入使用。由于吸附器吸附环境与再生环境差异较大,其由饱和切换至再生时需要进行至少包含减压、加热、冷却、升压在内的4个步骤,操控点多,管道布置和程控系统复杂,因此这种两台吸附器交替使用的工艺及其控制系统在实际运行过程中存在不少问题。阀门的误操作、程控阀故障、逻辑误判、纯化系统不正常切换以及管道布置不合理,会导致分子筛带水、吸附不完全、再生不彻底、放空管道积水等情况发生,对生产的经济性和安全性都带来巨大影响。可见,优化空分纯化工艺、精简纯化程控步骤是保持吸附剂优良吸附性能,提高空分纯化系统工作效率和经济性,减少事故发生的有效途径。The existing air separation plant purification system is generally composed of two switchable adsorbers (i.e., air purification devices), regenerative heating equipment, valves, pipelines, instrumentation and electronic controls, etc. During normal operation, one adsorber is adsorbed, and the other is regenerated. After one adsorption is saturated, the other regenerated adsorber will be put into use. Due to the large difference between the adsorption environment and the regeneration environment of the adsorber, at least four steps including decompression, heating, cooling, and boosting are required when switching from saturation to regeneration. There are many control points, and the pipeline layout and program control system are complicated. Therefore, there are many problems in the actual operation of the process of using two adsorbers alternately and its control system. Valve misoperation, program-controlled valve failure, logic misjudgment, abnormal switching of the purification system, and unreasonable pipeline layout will lead to water in the molecular sieve, incomplete adsorption, incomplete regeneration, water accumulation in the emptying pipeline, etc., which will affect the production economy. Both sex and security have huge implications. It can be seen that optimizing the air separation purification process and streamlining the purification program control steps is an effective way to maintain the excellent adsorption performance of the adsorbent, improve the working efficiency and economy of the air separation purification system, and reduce accidents.
发明内容Contents of the invention
为了解决上述现有技术存在的问题,本实用新型的目的在于提供一种转轮空分纯化装置,通过优化空分纯化系统的工艺流程从而简化其程控系统来降低故障发生率,以保持吸附剂优良的吸附性能,提高空分纯化系统工作效率,延长空分设备寿命。In order to solve the problems existing in the above-mentioned prior art, the purpose of this utility model is to provide a rotary air separation and purification device, by optimizing the process flow of the air separation and purification system to simplify its program control system to reduce the incidence of failure, so as to keep the adsorbent Excellent adsorption performance, improve the working efficiency of the air separation purification system, and prolong the life of the air separation equipment.
为达到以上目的,本实用新型采用如下技术方案:In order to achieve the above object, the utility model adopts the following technical solutions:
一种转轮空分纯化装置,包括依次连接的空气过滤器1、空气压缩机2、空气预冷塔3、空气纯化装置4和空气增压机5,所述空气纯化装置4包括相间隔的空气管道、再生热风管道和再生冷风管道,还包括转轮型吸附器6以及与转轮型吸附器6连接并控制其旋转的转动电机7,所述转轮型吸附器6将空气管道、再生热风管道和再生冷风管道分为上下两部分,同时空气管道、再生热风管道和再生冷风管道将转轮型吸附器6分别分为吸附区14、再生加热区15和再生冷却区16,所述吸附区14、再生加热区15和再生冷却区16中均匀布置有多个仓格板17,所述仓格板17间装有吸附剂18;所述空气管道的下部分为和空气预冷塔3连接的空气入口管道8,上部分为和空气增压机5连接的空气出口管道9,所述再生热风管道的上部分为再生热风入口管道10,下部分为再生热风出口管道11,所述再生冷风管道的上部分为再生冷风入口管道12,下部分为再生冷风出口管道13。A kind of wheel air separation and purification device comprises an air filter 1, an air compressor 2, an air precooling tower 3, an air purification device 4 and an air booster 5 connected in sequence, and the air purification device 4 includes spaced apart The air duct, the regenerative hot air duct and the regenerative cold air duct also include a rotor-type adsorber 6 and a rotating motor 7 connected with the rotor-type adsorber 6 and controlling its rotation. The hot air duct and the regenerative cold air duct are divided into upper and lower parts. At the same time, the air duct, the regenerative hot air duct and the regenerative cold air duct divide the runner-type adsorber 6 into an adsorption zone 14, a regenerative heating zone 15 and a regenerative cooling zone 16. In the zone 14, the regenerative heating zone 15 and the regenerative cooling zone 16, there are a plurality of grid plates 17 evenly arranged, and the adsorbent 18 is installed between the grid plates 17; the lower part of the air pipeline is divided into the air precooling tower 3 Connected air inlet pipeline 8, the upper part is the air outlet pipeline 9 connected with the air booster 5, the upper part of the regeneration hot air pipeline is the regeneration hot blast inlet pipeline 10, and the lower part is the regeneration hot blast outlet pipeline 11. The upper part of the cold air duct is the regenerative cold air inlet duct 12 , and the lower part is the regenerative cold air outlet duct 13 .
所述转轮型吸附器6为单层或双层结构。The rotary adsorber 6 is a single-layer or double-layer structure.
所述转轮型吸附器6为双层结构,下层设置活性氧化铝;上层设置分子筛。The wheel-type adsorber 6 has a double-layer structure, the lower layer is provided with activated alumina, and the upper layer is provided with molecular sieves.
所述吸附区14、再生加热区15和再生冷却区16的面积为2:1:1。The area of the adsorption zone 14 , the regeneration heating zone 15 and the regeneration cooling zone 16 is 2:1:1.
所述空气管道、再生热风管道和再生冷风管道与转轮型吸附器6间采用旋转机械密封。Rotary mechanical seals are used between the air duct, regeneration hot air duct and regeneration cold air duct and the runner-type adsorber 6 .
所述旋转机械密封采用柔性接触式密封、双密封或刷式密封。The rotary mechanical seal adopts flexible contact seal, double seal or brush seal.
所述空气过滤器1为自洁式空气过滤器。The air filter 1 is a self-cleaning air filter.
本实用新型和现有技术相比,具有如下优点:Compared with the prior art, the utility model has the following advantages:
1)本实用新型属于去除空气中杂质的装置,通过物理吸附、再生等过程实现空气中二氧化碳、碳水化合物及水蒸汽大量、高效率地脱除,保证空气的纯净干燥。1) The utility model belongs to a device for removing impurities in the air. Through physical adsorption, regeneration and other processes, a large amount of carbon dioxide, carbohydrates and water vapor in the air can be removed with high efficiency to ensure that the air is pure and dry.
2)通过将吸附器设置成转轮结构,在转轮周围形成吸附区、再生加热区和再生冷却区,转轮在旋转过程中依次缓慢通过这三个区域。相比于两台吸附剂切换使用的工艺流程,本实用新型将吸附剂的吸附、再生过程变成连续进行的,某吸附区面积大小的吸附剂从完全的吸附环境进入到完全再生环境有一个缓慢适应的过程,无需进行升、降压操作,从而简化了程控步骤,减少了程控阀门数量,降低了因阀门误操作、程控阀故障、逻辑误判或管道布置不合理所造成的分子筛带水、吸附不完全、再生不彻底、放空管道积水等情况发生的几率,极大地提高了空分系统可靠性和经济性,从而延长设备寿命。2) By setting the adsorber as a runner structure, an adsorption zone, a regeneration heating zone and a regeneration cooling zone are formed around the runner, and the runner slowly passes through these three regions in turn during rotation. Compared with the technological process of switching between two adsorbents, the utility model makes the adsorption and regeneration process of the adsorbent continuous, and the adsorbent with a certain size of the adsorption area enters the complete regeneration environment from a complete adsorption environment to a complete regeneration environment. The process of slow adaptation does not need to increase or decrease the pressure, thus simplifying the program control steps, reducing the number of program control valves, and reducing the molecular sieve carrying water caused by valve misoperation, program control valve failure, logic misjudgment or unreasonable pipeline layout , Incomplete adsorption, incomplete regeneration, and water accumulation in emptying pipelines, etc., greatly improve the reliability and economy of the air separation system, thereby prolonging the life of the equipment.
3)本实用新型装置结构紧凑,吸附区、再生加热区和再生冷却区在空间上紧密相连,无需复杂的旁路管道及放空管道连接,既提高了空分纯化系统工作效率,又节省了空分纯化系统的占地空间以及制造成本。3) The device of the utility model has a compact structure, and the adsorption area, the regeneration heating area and the regeneration cooling area are closely connected in space, and there is no need for complicated bypass pipes and vent pipe connections, which not only improves the working efficiency of the air separation and purification system, but also saves space. The floor space and manufacturing cost of the separation and purification system.
4)结构简单,简化了工艺操作和控制流程,便于运行人员理解和操控,可有效降低运行风险,增加生产效率。4) The structure is simple, the process operation and control process are simplified, and it is easy for the operator to understand and control, which can effectively reduce the operation risk and increase the production efficiency.
附图说明Description of drawings
图1为本实用新型转轮空分纯化装置结构及流程示意图。Fig. 1 is the structure and flow diagram of the utility model runner air separation and purification device.
图2为空气纯化装置俯视结构示意图。Figure 2 is a schematic top view of the air purification device.
图3为空气纯化装置仰视结构示意图。Figure 3 is a schematic diagram of the structure of the air purification device viewed from the bottom.
其中,in,
1——空气过滤器;2——空气压缩机;3——空气预冷塔;4——空气纯化装置;5——空气增压机;6——转轮型吸附器;7——转动电机;8——空气入口管道;9——空气出口管道;10——再生热风入口管道;11——再生热风出口管道;12——再生冷风入口管道;13——再生冷风出口管道;14——吸附区;15——再生加热区;16——再生冷却区;17——仓格板;18——吸附剂。1—air filter; 2—air compressor; 3—air precooling tower; 4—air purification device; 5—air booster; 6—rotary adsorber; 7—rotation Motor; 8—air inlet pipe; 9—air outlet pipe; 10—regeneration hot air inlet pipe; 11—regeneration hot air outlet pipe; 12—regeneration cold air inlet pipe; 13—regeneration cold air outlet pipe; 14— — Adsorption area; 15 — Regeneration heating area; 16 — Regeneration cooling area; 17 — Storage grid; 18 — Adsorbent.
具体实施方式Detailed ways
以下结合附图及具体实施例,对本实用新型作进一步的详细描述。Below in conjunction with accompanying drawing and specific embodiment, the utility model is described in further detail.
如图1、图2和图3所示,本实用新型一种转轮空分纯化装置,包括依次连接的空气过滤器1、空气压缩机2、空气预冷塔3、空气纯化装置4和空气增压机5,所述空气纯化装置4包括相间隔的空气管道、再生热风管道和再生冷风管道,还包括转轮型吸附器6以及与转轮型吸附器6连接并控制其旋转的转动电机7,所述转轮型吸附器6将空气管道、再生热风管道和再生冷风管道分为上下两部分,同时空气管道、再生热风管道和再生冷风管道将转轮型吸附器6分别分为吸附区14、再生加热区15和再生冷却区16,所述吸附区14、再生加热区15和再生冷却区16中均匀布置有多个仓格板17,所述仓格板17间装有吸附剂18;所述空气管道的下部分为和空气预冷塔3连接的空气入口管道8,上部分为和空气增压机5连接的空气出口管道9,所述再生热风管道的上部分为再生热风入口管道10,下部分为再生热风出口管道11,所述再生冷风管道的上部分为再生冷风入口管道12,下部分为再生冷风出口管道13。空气经空气压缩机2增压到0.6MPa后自下而上穿过空气预冷塔3,在温度由350K冷却至310K的同时,又得到清洗。之后空气进入纯化装置4空气入口管道,通过转轮型吸附器6,空气中的二氧化碳、碳水化合物及残留的水蒸汽被吸附。净化后的空气经空气增压机5增压后去往空分系统其他环节As shown in Fig. 1, Fig. 2 and Fig. 3, a kind of wheel air separation and purification device of the present invention comprises an air filter 1, an air compressor 2, an air precooling tower 3, an air purification device 4 and an air Supercharger 5, said air purification device 4 includes spaced air ducts, regenerative hot air ducts and regenerative cold air ducts, and also includes a rotor-type adsorber 6 and a rotating motor connected to the rotor-type adsorber 6 and controlling its rotation 7. The runner-type adsorber 6 divides the air duct, regeneration hot-air duct and regeneration cold-air duct into upper and lower parts, while the air duct, regeneration hot-air duct and regeneration cold-air duct divide the rotor-type adsorber 6 into adsorption zones respectively 14. The regeneration heating zone 15 and the regeneration cooling zone 16, the adsorption zone 14, the regeneration heating zone 15 and the regeneration cooling zone 16 are evenly arranged with a plurality of compartment panels 17, and the compartment panels 17 are equipped with adsorbents 18 The lower part of the air duct is the air inlet duct 8 connected with the air precooling tower 3, the upper part is the air outlet duct 9 connected with the air booster 5, and the upper part of the regeneration hot blast pipeline is the regeneration hot blast inlet The lower part of the pipe 10 is a regenerated hot air outlet pipe 11 , the upper part of the regenerated cold air pipe is a regenerated cold air inlet pipe 12 , and the lower part is a regenerated cold air outlet pipe 13 . The air is pressurized to 0.6MPa by the air compressor 2, and then passes through the air precooling tower 3 from bottom to top, and is cleaned while the temperature is cooled from 350K to 310K. Afterwards, the air enters the air inlet pipeline of the purification device 4, and passes through the rotor type adsorber 6, and carbon dioxide, carbohydrates and residual water vapor in the air are adsorbed. The purified air goes to other links of the air separation system after being pressurized by the air booster 5
所述转轮型吸附器6为单层或双层结构。优选地,对于大型空分纯化系统,所述转轮型吸附器6为双层结构,下层装填500mm活性氧化铝,利用其对空气进行初步干燥;上层填装1000mm分子筛,可以有选择性地吸附二氧化碳、水分及碳氢化合物等杂质。下层氧化铝床层代替分子筛吸附水分,可以有效地保护分子筛,增大分子筛吸附其它杂质的容量,延长分子筛使用寿命。The rotary adsorber 6 is a single-layer or double-layer structure. Preferably, for a large-scale air separation and purification system, the rotor-type adsorber 6 is a double-layer structure, the lower layer is filled with 500mm activated alumina, and the air is initially dried by using it; the upper layer is filled with a 1000mm molecular sieve, which can selectively adsorb Impurities such as carbon dioxide, moisture, and hydrocarbons. The lower alumina bed replaces the molecular sieve to absorb water, which can effectively protect the molecular sieve, increase the capacity of the molecular sieve to absorb other impurities, and prolong the service life of the molecular sieve.
作为本实用新型的优选实施方式,所述吸附区14、再生加热区15和再生冷却区16的面积为2:1:1。As a preferred embodiment of the present invention, the area of the adsorption zone 14 , the regeneration heating zone 15 and the regeneration cooling zone 16 is 2:1:1.
作为本实用新型的优选实施方式,所述空气管道、再生热风管道和再生冷风管道与转轮型吸附器6间采用旋转机械密封。As a preferred embodiment of the present utility model, a rotary mechanical seal is used between the air duct, the regeneration hot air duct and the regeneration cold air duct and the rotor-type adsorber 6 .
作为本实用新型进一步的优选实施方式,所述旋转机械密封采用柔性接触式密封、双密封或刷式密封。As a further preferred embodiment of the present invention, the rotary mechanical seal adopts flexible contact seal, double seal or brush seal.
作为本实用新型的优选实施方式,所述空气过滤器1为自洁式空气过滤器。As a preferred embodiment of the present utility model, the air filter 1 is a self-cleaning air filter.
本实用新型的工作原理为:空气经空气过滤器1过滤并经空气压缩机2增压后,自下而上穿过空气预冷塔3,从空气入口管道8进入吸附区14,先由活性氧化铝吸附水分,再由分子筛吸附二氧化碳、乙炔杂质,空气中的二氧化碳、碳水化合物及水蒸汽被吸附从而变为纯净的空气,纯净的空气通过空气出口管道9进入空气增压机5;与此同时,转轮型吸附器6在转动电机7的带动下以缓慢的速度不停转动,当吸收二氧化碳、碳水化合物及水蒸汽的吸附剂18随转轮型吸附器6转动到再生加热区15时,自再生热风入口管道10来的热风会对吸附剂18进行加温解吸,从而将吸附剂18吸附的杂质带走,通过再生热风出口管道11排出;脱吸后的吸附剂18随转轮型吸附器6转动到再生冷却区16,自再生冷风入口管道12来的冷风会对其进行冷吹,从而将吸附剂18冷却下来;冷却风则穿过吸附剂18通过再生冷风出口管道13排出,吸附器18完成一个吸附与再生周期。The working principle of the utility model is: after the air is filtered by the air filter 1 and pressurized by the air compressor 2, it passes through the air pre-cooling tower 3 from bottom to top, enters the adsorption area 14 from the air inlet pipe 8, and is first activated by the active Alumina absorbs water, and then molecular sieves absorb carbon dioxide and acetylene impurities. Carbon dioxide, carbohydrates and water vapor in the air are absorbed to become pure air, and the pure air enters the air booster 5 through the air outlet pipe 9; Simultaneously, the runner-type adsorber 6 is driven by the rotating motor 7 and rotates continuously at a slow speed. , the hot air from the regenerative hot air inlet pipe 10 will heat and desorb the adsorbent 18, thereby taking away the impurities adsorbed by the adsorbent 18, and discharge them through the regenerated hot air outlet pipe 11; The adsorber 6 rotates to the regenerative cooling zone 16, and the cold wind from the regenerative cold air inlet pipe 12 will blow it coldly, thereby cooling the adsorbent 18; The adsorber 18 completes an adsorption and regeneration cycle.
作为本实用新型的优选实施方式,所述转轮型吸附器6在转动电机7的带动下以0.25πrad/h的角速度顺时针匀速转动,转动周期为8h。As a preferred embodiment of the present invention, the wheel-type adsorber 6 is driven by the rotating motor 7 to rotate clockwise at a constant speed of 0.25πrad/h, and the rotation period is 8h.
所述热风成分为高温干燥的氮气、氧气和氩气中的一种或多种混合气,温度在150℃至200℃之间;所述冷风成分为常温干燥的氮气、氧气和氩气中的一种或多种混合气,温度在10℃至20℃之间。The hot air component is one or more mixtures of high-temperature dry nitrogen, oxygen and argon, and the temperature is between 150 ° C and 200 ° C; the cold air component is normal temperature dry nitrogen, oxygen and argon One or more mixed gases, the temperature is between 10°C and 20°C.
本实用新型方法通过优化空气纯化工艺流程来简化空气纯化系统的程控系统及管道阀门布置。与常规空气纯化方法相比,该方法不仅减少了占地空间、简化了管道布置、节约了成本,还在保持良好吸附性能的前提下减少了因阀门误操作、程控阀故障、逻辑误判或管道布置不合理所带来的安全风险。应用该方法运行足够长一段时间后,无任何分子筛带水、吸附不完全、再生不彻底、放空管道积水等情况的发生,经纯化后的空气二氧化碳等杂质含量一直低于1ppm。由于可以一直运行在这种良好状况下,本实用新型方法可将分子筛及相关设备寿命延长1至2年。The method of the utility model simplifies the program control system and pipeline valve arrangement of the air purification system by optimizing the air purification process flow. Compared with conventional air purification methods, this method not only reduces floor space, simplifies pipeline layout, and saves costs, but also reduces the risk of valve misoperation, program-controlled valve failure, logic misjudgment or Safety risks caused by unreasonable pipeline layout. After applying this method for a long enough period of time, there is no occurrence of any molecular sieve carrying water, incomplete adsorption, incomplete regeneration, and water accumulation in the emptying pipeline, and the content of impurities such as carbon dioxide in the purified air has always been lower than 1ppm. Owing to being able to operate under such good conditions all the time, the method of the utility model can prolong the service life of molecular sieves and related equipment by 1 to 2 years.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN104208980A (en) * | 2014-08-22 | 2014-12-17 | 中国华能集团清洁能源技术研究院有限公司 | Turning wheel air separation purification device and turning wheel air separation purification method |
CN106731478A (en) * | 2015-11-24 | 2017-05-31 | 杰智环境科技股份有限公司 | Horizontal runner and fluid purification processing system |
CN108096990A (en) * | 2016-11-25 | 2018-06-01 | 中国石油化工股份有限公司 | A kind of adsorption separation device |
CN108273360A (en) * | 2018-01-29 | 2018-07-13 | 神华集团有限责任公司 | CO2Continuous rotary adsorption system and method |
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2014
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104208980A (en) * | 2014-08-22 | 2014-12-17 | 中国华能集团清洁能源技术研究院有限公司 | Turning wheel air separation purification device and turning wheel air separation purification method |
CN106731478A (en) * | 2015-11-24 | 2017-05-31 | 杰智环境科技股份有限公司 | Horizontal runner and fluid purification processing system |
CN108096990A (en) * | 2016-11-25 | 2018-06-01 | 中国石油化工股份有限公司 | A kind of adsorption separation device |
CN108273360A (en) * | 2018-01-29 | 2018-07-13 | 神华集团有限责任公司 | CO2Continuous rotary adsorption system and method |
CN108273360B (en) * | 2018-01-29 | 2020-10-23 | 神华集团有限责任公司 | CO2Continuous rotary adsorption system and method |
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