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CN208194040U - Hypergravity moves adsorbent bed adsorbed gas equipment - Google Patents

Hypergravity moves adsorbent bed adsorbed gas equipment Download PDF

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CN208194040U
CN208194040U CN201820467668.0U CN201820467668U CN208194040U CN 208194040 U CN208194040 U CN 208194040U CN 201820467668 U CN201820467668 U CN 201820467668U CN 208194040 U CN208194040 U CN 208194040U
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adsorption
adsorbent
bed
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adsorption column
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刘有智
郭强
祁贵生
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North University of China
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Abstract

本实用新型属于固体吸附剂吸附气体的吸附、脱附技术领域,为解决传统吸附床吸附、脱附效果差,吸附剂利用率低等问题,提供了一种一种超重力移动吸附床吸附气体设备。本实用新型有三种模式,包括固定床模式、移动床模式和旋转床模式,所述设备包括吸附柱,吸附柱中装有吸附剂,通过改变吸附剂在吸附柱中的流速和吸附柱的转速来改变设备的模式。模式转换是在同一设备装置中进行,实现了高效、连续性操作。本实用新型可以大大提高吸附剂的利用率,缩短饱和吸附剂的脱附再生时间,处理效果高、运行成本低,提高了吸附剂寿命同时,改善了吸附设备的吸附性能,具有一定的工程实际应用意义和节能环保意义。

The utility model belongs to the technical field of adsorption and desorption of gases adsorbed by solid adsorbents. In order to solve the problems of poor adsorption and desorption effects of traditional adsorption beds and low utilization rate of adsorbents, the utility model provides a supergravity mobile adsorption bed for adsorbing gases. equipment. The utility model has three modes, including a fixed bed mode, a moving bed mode and a rotating bed mode. The equipment includes an adsorption column, and an adsorbent is installed in the adsorption column. By changing the flow rate of the adsorbent in the adsorption column and the rotational speed of the adsorption column, to change the mode of the device. Mode switching is carried out in the same equipment unit, realizing efficient and continuous operation. The utility model can greatly improve the utilization rate of the adsorbent, shorten the desorption regeneration time of the saturated adsorbent, have high treatment effect, low operating cost, increase the life of the adsorbent, and improve the adsorption performance of the adsorption equipment at the same time, which has certain engineering practice Application significance and significance of energy saving and environmental protection.

Description

超重力移动吸附床吸附气体设备High gravity mobile adsorption bed adsorption gas equipment

技术领域technical field

本实用新型属于固体吸附剂吸附气体的吸附、脱附技术领域,具体涉及一种超重力移动吸附床吸附气体设备。The utility model belongs to the technical field of adsorption and desorption of gases adsorbed by solid adsorbents, and in particular relates to a gas adsorption device for a supergravity mobile adsorption bed.

背景技术Background technique

吸附是一种重要的化工单元操作过程,广泛应用于石油、化工、冶金、食品、医药等方面,在日常生活和工业生产中,吸附还应用于家用净水、冰箱除异味等方面。吸附是流动相与多孔的固体颗粒接触,使固体颗粒有选择性地累积和凝聚流动相中一定组分在其内外表面上,从而达到分离目的。常见的吸附剂有硅胶、活性氧化铝、活性炭和分子筛等,可以根据所处理的流动相进行合理选择。提高吸附率的主要手段是对吸附设备进行改进,通过改变流动相和吸附剂的接触方式,提高吸附剂的吸附及再生能力。工业上通常采用的吸附设备有吸附槽、固定床、流化床和移动床。Adsorption is an important chemical unit operation process, widely used in petroleum, chemical industry, metallurgy, food, medicine, etc. In daily life and industrial production, adsorption is also used in household water purification, refrigerator deodorization, etc. Adsorption is the contact between the mobile phase and porous solid particles, so that the solid particles selectively accumulate and condense certain components in the mobile phase on their inner and outer surfaces, so as to achieve the purpose of separation. Common adsorbents include silica gel, activated alumina, activated carbon, and molecular sieve, which can be reasonably selected according to the mobile phase to be processed. The main means to improve the adsorption rate is to improve the adsorption equipment, and improve the adsorption and regeneration capacity of the adsorbent by changing the contact mode between the mobile phase and the adsorbent. Adsorption equipment commonly used in industry includes adsorption tank, fixed bed, fluidized bed and moving bed.

固定床属于间歇操作,整个吸附过程中非吸附时间较长,若吸附浆液或粘稠液时,很容易堵塞床层,吸附剂固定在床层中,靠吸附质穿梭其中,吸附剂的利用率较低。流化床中的吸附剂处于湍动状态,在吸附过程中吸附效率虽高,但返混严重,吸附剂磨损厉害,对吸附剂质量要求较高。移动床中吸附颗粒有序向下移动,与进料物系逆流接触,该装置操作连续化,提高了吸附剂的利用率,增加了原料处理。对高浓度的吸附介质仍具有一定的吸附能力。移动床具有吸附效率高、处理量大等优点,广泛应用于工业生产中。The fixed bed belongs to intermittent operation, and the non-adsorption time in the whole adsorption process is long. If the slurry or viscous liquid is adsorbed, it is easy to block the bed layer. The adsorbent is fixed in the bed layer, and the adsorbate shuttles through it. lower. The adsorbent in the fluidized bed is in a turbulent state. Although the adsorption efficiency is high during the adsorption process, the back-mixing is serious, and the adsorbent is severely worn, which requires high quality of the adsorbent. The adsorption particles in the moving bed move down in an orderly manner and contact with the feed material system countercurrently. The operation of the device is continuous, which improves the utilization rate of the adsorbent and increases the raw material treatment. It still has a certain adsorption capacity for high-concentration adsorption media. The moving bed has the advantages of high adsorption efficiency and large processing capacity, and is widely used in industrial production.

吸附要有相应的脱附技术与之相对应,传统的吸附设备进行脱附工艺时,存在脱附效率低、脱附时间长等劣势,与相应的吸附过程不相匹配。旋转填料床是一种新型、高效气质传质设备,在强化传质方面有广泛的应用,可以提高脱附率,缩短脱附时间,为吸附提供充足的新鲜吸附剂。Adsorption requires a corresponding desorption technology to correspond to it. When the traditional adsorption equipment performs the desorption process, there are disadvantages such as low desorption efficiency and long desorption time, which do not match the corresponding adsorption process. Rotating packed bed is a new type of high-efficiency gas mass transfer equipment. It has been widely used in enhancing mass transfer. It can increase the desorption rate, shorten the desorption time, and provide sufficient fresh adsorbent for adsorption.

寻求一种高效的吸附、脱附设备,并将其一体化,实现连续运行,对不同浓度的吸附介质采用与之匹配的吸附设备,是目前吸附工段方面急需迫切解决的问题,本实用新型所述的超重力移动吸附床吸附气体设备,可以有效解决吸附、脱附方面存在的问题,提升了生产效率。Seeking for an efficient adsorption and desorption equipment, and integrating it to realize continuous operation, and using matching adsorption equipment for adsorption media with different concentrations is an urgent problem that needs to be solved urgently in the adsorption section. The above-mentioned high-gravity moving adsorption bed adsorption gas equipment can effectively solve the problems existing in adsorption and desorption, and improve production efficiency.

发明内容Contents of the invention

本实用新型为了解决各类型传统吸附床存在的一些问题,如固定床吸附剂利用率低,吸附效果差,流化床存在返混严重,吸附剂易磨损问题,工业吸附床属于间歇操作,造成工艺运行不稳定等问题;另一方面,对于饱和吸附剂的脱附过程,固定床脱附时间长、脱附效果极差。针对以上问题,提出了一种超重力移动吸附床吸附气体设备,有效解决吸附、脱附过程中存在的问题。The utility model aims to solve some problems existing in various types of traditional adsorption beds, such as low utilization rate of fixed bed adsorbent, poor adsorption effect, serious back-mixing in fluidized bed, easy wear of adsorbent, industrial adsorption bed belongs to intermittent operation, resulting in On the other hand, for the desorption process of saturated adsorbent, the desorption time of fixed bed is long and the desorption effect is extremely poor. In view of the above problems, a high-gravity moving adsorption bed adsorption gas equipment is proposed, which can effectively solve the problems existing in the adsorption and desorption process.

本实用新型采用如下技术方案实现:The utility model adopts following technical scheme to realize:

一种超重力移动吸附床吸附气体设备,其特征在于所述设备有三种模式,包括固定床模式、移动床模式和旋转床模式,所述设备包括吸附柱,吸附柱中装有吸附剂,通过改变吸附剂在吸附柱中的流速和吸附柱的转速来改变设备的模式。A high-gravity mobile adsorption bed adsorption gas equipment is characterized in that the equipment has three modes, including fixed bed mode, moving bed mode and rotating bed mode, the equipment includes an adsorption column, and the adsorption column is equipped with an adsorbent. Change the flow rate of the adsorbent in the adsorption column and the rotation speed of the adsorption column to change the mode of the equipment.

进一步的,所述吸附柱轴向连接电机,吸附柱底部有进气口、还有吸附剂出口,吸附柱顶部有加料口,所述固定床模式,电机关闭,吸附剂封闭在吸附柱内;所述移动床模式,电机低速转动、吸附剂出口打开、顶部加料口填加吸附剂,吸附剂在吸附柱内自上而下流动;所述旋转床模式,电机高速转动、吸附剂封闭在吸附柱内。Further, the adsorption column is axially connected to the motor, the bottom of the adsorption column has an air inlet and an adsorbent outlet, and the top of the adsorption column has a feeding port. In the fixed bed mode, the motor is turned off, and the adsorbent is enclosed in the adsorption column; In the moving bed mode, the motor rotates at low speed, the adsorbent outlet is opened, and the top feeding port is filled with adsorbent, and the adsorbent flows from top to bottom in the adsorption column; in the rotating bed mode, the motor rotates at high speed, and the adsorbent is closed in the adsorption column. inside the column.

进一步的,所述设备底部设有吸附剂收集口,吸附柱底部的吸附剂出口至吸附剂收集口,由螺旋板顺式下滑,整个吸附和回收过程处在密封环境中。Further, the bottom of the device is provided with an adsorbent collection port, and the adsorbent outlet at the bottom of the adsorption column goes down to the adsorbent collection port, and slides down through the spiral plate, and the entire adsorption and recovery process is in a sealed environment.

进一步的,所述吸附柱底部装有气体分布器,气体经气体分布器进入吸附柱内部,其所述的气体分布器为圆锥形设计,锥面上设有微孔,所述的气体分布器与吸附柱同轴线。Further, a gas distributor is installed at the bottom of the adsorption column, and the gas enters the interior of the adsorption column through the gas distributor. The gas distributor is conical in design, and micropores are provided on the cone surface. The gas distributor Coaxial with adsorption column.

进一步的,所述的吸附剂出口与吸附柱轴线呈角度设置,吸附剂出口位于气体分布器上方,吸附剂出口处设置有调节阀。Further, the adsorbent outlet is set at an angle to the axis of the adsorption column, the adsorbent outlet is located above the gas distributor, and a regulating valve is arranged at the adsorbent outlet.

进一步的,所述的所述的设备两台串联使用,吸附、脱附连续化运行;其中一台完成吸附过程后,直接通入吹脱气,调高转速,直接进行脱附过程,同时另一台进行吸附过程。Further, two of the above-mentioned devices are used in series, and the adsorption and desorption are operated continuously; after the adsorption process is completed in one of them, it is directly fed into the degassing and degassing, the speed is increased, and the desorption process is directly carried out, while the other One for the adsorption process.

所述的超重力移动吸附床吸附气体设备完成的气体处理过程,包括如下:The gas treatment process completed by the high-gravity moving adsorption bed adsorption gas equipment includes the following:

1)、所述设备为固定床模式,关闭电机,吸附剂出口为关闭状态,废气由下至上进入吸附柱进行吸附,适用于处理低浓度废气;1) The device is in fixed bed mode, the motor is turned off, the outlet of the adsorbent is closed, and the waste gas enters the adsorption column from bottom to top for adsorption, which is suitable for treating low-concentration waste gas;

2)、所述设备为移动床模式,将电机转速调至低速状态,废气由下至上进入吸附柱,吸附剂缓慢地由上而下通过吸附柱,废气与吸附剂逆流接触,完成吸附过程,在整个过程中,新鲜吸附剂不断的从吸附柱上端的加料口中加入,完成吸附的吸附剂从吸附柱底部两侧的吸附剂出口甩出,由螺旋板导流入吸附剂收集口,适用于处理高浓度废气;2) The equipment is in the moving bed mode, the motor speed is adjusted to a low speed state, the exhaust gas enters the adsorption column from bottom to top, and the adsorbent slowly passes through the adsorption column from top to bottom, and the exhaust gas and the adsorbent are in countercurrent contact to complete the adsorption process. During the whole process, fresh adsorbent is continuously added from the feeding port at the upper end of the adsorption column, and the adsorbent that has been completely adsorbed is thrown out from the adsorbent outlets on both sides of the bottom of the adsorption column, and guided by the spiral plate into the adsorbent collection port, which is suitable for processing High concentration exhaust gas;

3)、旋转床模式,电机高速转动,吸附剂出口为关闭状态,吸附柱上端加料口也为关闭状态,废气由下至上进入吸附柱进行吸附;3) Rotating bed mode, the motor rotates at high speed, the outlet of the adsorbent is closed, the feeding port at the upper end of the adsorption column is also closed, and the waste gas enters the adsorption column from bottom to top for adsorption;

4)、上述1)、2)、3)三种模式,将吸附剂更换为吸附饱和的吸附剂,废气更换为吹脱气,其他反应条件不变,进行脱附过程。4) In the above three modes of 1), 2), and 3), the adsorbent is replaced with a saturated adsorbent, the waste gas is replaced with degassing, and the other reaction conditions remain unchanged, and the desorption process is carried out.

进一步的,所述脱附过程选用旋转床模式。Further, the desorption process adopts the rotating bed mode.

进一步的,所述移动床模式下电机转速为0-50r/min,所述旋转床模式下电机转速为100-500r/min。Further, the motor speed in the moving bed mode is 0-50r/min, and the motor speed in the rotating bed mode is 100-500r/min.

进一步的,所述的吸附剂是活性炭、活性氧化铝、硅胶、分子筛等,所述的吹脱气是水蒸气、热空气、氮气等。Further, the adsorbent is activated carbon, activated alumina, silica gel, molecular sieve, etc., and the degassing gas is water vapor, hot air, nitrogen, etc.

进一步的,所述的进气口包括吹脱气进口和废气进口。Further, the air inlet includes a stripping gas inlet and a waste gas inlet.

本实用新型实现了不同类型吸附床一体化,包括固定床、移动床和旋转床的一体化,采用各种模式分别进行吸附和饱和吸附剂脱附过程,实现高效、连续的吸附、再脱附过程。本实用新型单台使用为间歇式操作;若两台串联使用,可以实现吸附、脱附连续化运行,吸附过程完成后,直接通入吹脱气,调高转速,直接进行脱附过程,减少了工序,提高了生产效率。脱附剂可采用工业上的水蒸气或者工业余热的热空气,即可以节省能源,又充分利用工业资源。本实用新型适合处理挥发性有机气体和一些有毒、有害恶臭气体等。采用本实用新型进行吸附,可以大大提高吸附剂的利用率,缩短饱和吸附剂的脱附再生时间,处理效果高、运行成本低,提高了吸附剂寿命同时,改善了吸附设备的吸附性能,具有一定的工程实际应用意义和节能环保意义。The utility model realizes the integration of different types of adsorption beds, including the integration of fixed beds, moving beds and rotating beds, adopts various modes to carry out the adsorption and desorption processes of saturated adsorbents, and realizes efficient and continuous adsorption and re-desorption process. The utility model uses a single unit for intermittent operation; if two units are used in series, it can realize continuous operation of adsorption and desorption. The process is simplified and the production efficiency is improved. The desorbent can use industrial water vapor or hot air from industrial waste heat, which can save energy and make full use of industrial resources. The utility model is suitable for processing volatile organic gases and some poisonous and harmful odorous gases and the like. Adopting the utility model for adsorption can greatly improve the utilization rate of the adsorbent, shorten the desorption regeneration time of the saturated adsorbent, have high treatment effect, low operating cost, increase the life of the adsorbent, and improve the adsorption performance of the adsorption equipment at the same time. Certain engineering practical application significance and energy conservation and environmental protection significance.

附图说明Description of drawings

图1是本实用新型所述超重力移动吸附床吸附气体设备的装置示意图;Fig. 1 is the device schematic diagram of the supergravity moving adsorption bed adsorption gas equipment described in the utility model;

图2是本实用新型所述气体分布器以及气体分布器示意图;Fig. 2 is a schematic diagram of the gas distributor and the gas distributor of the utility model;

图1中:1-吹脱气进口;2-废气进口;3-气封装置;4-吸附剂出口;5-气体分布器;6-吸附柱;7-密封盖;8-螺旋板;9-吸附剂收集口;10-电机。In Fig. 1: 1- stripping gas inlet; 2- waste gas inlet; 3- gas sealing device; 4- adsorbent outlet; 5- gas distributor; 6- adsorption column; 7- sealing cover; 8- spiral plate; 9 - Sorbent collection port; 10 - Motor.

具体实施方式Detailed ways

结合附图对本实用新型的具体实施方式做进一步说明。The specific embodiment of the utility model will be further described in conjunction with the accompanying drawings.

超重力移动吸附床吸附气体设备,为固定床、移动床和旋转床一体化设备,吸附床模式的转换通过改变电机频率实现。固定床模式是在电机停滞状态下进行,吸附剂出口为关闭状态,废气从底部气体进口通入,由下至上完成气体吸附过程。移动床模式是在电机的低频率带动下低速旋转,吸附剂从吸附柱两侧吸附剂出口缓慢流出,由螺旋板引流至底部吸附剂收集口,新鲜吸附剂从吸附柱上端加料口加入,废气从进气口通入,由下向上进入吸附柱,与由上而下的吸附剂充分接触,完成吸附过程,整个吸附过程,在密闭环境下进行。旋转床模式是在吸附剂出口闭合,电机频率较高情况下进行吸附;吸附完成后,将吸附剂出口封闭,吸附柱上端加料口封住,底部进气口通入吹脱气,在电机的旋转带动下进行脱附过程。The high-gravity mobile adsorption bed adsorption gas equipment is an integrated equipment of fixed bed, moving bed and rotating bed. The conversion of the adsorption bed mode is realized by changing the frequency of the motor. The fixed bed mode is carried out when the motor is stagnant, the outlet of the adsorbent is closed, and the exhaust gas is introduced from the bottom gas inlet, and the gas adsorption process is completed from bottom to top. The moving bed mode is driven by the low frequency of the motor to rotate at a low speed. The adsorbent flows out slowly from the adsorbent outlets on both sides of the adsorption column, and is drained by the spiral plate to the adsorbent collection port at the bottom. Fresh adsorbent is added from the feeding port at the upper end of the adsorption column. It enters from the air inlet, enters the adsorption column from bottom to top, and fully contacts with the adsorbent from top to bottom to complete the adsorption process. The entire adsorption process is carried out in a closed environment. The rotating bed mode is to adsorb when the adsorbent outlet is closed and the frequency of the motor is high; The desorption process is carried out under the driving of rotation.

待处理的气体经过除杂、净化后,利用本实用新型完成气体吸附过程,根据吸附介质浓度不同,选择合适的吸附床类型。包括如下:1)对于低浓度废气,关闭电机,设备保持为固定床模式,吸附柱内装填有吸附剂,吸附剂处于静止状态,待处理气体由下至上进入吸附柱进行吸附;2)对于高浓度废气,将转速调至低速状态,设备保持为移动床模式,待处理废气通入床内,吸附剂缓慢的由上而下通过吸附柱,与由下至上的气体逆流接触,完成吸附过程。在整个过程中,新鲜吸附剂不断的从上方加料口中加入,吸附完成的吸附剂从吸附柱两侧甩出,由螺旋板流入吸附剂收集口。吸附剂与废气逆流接触,极大地增加了接触面积,使气体和吸附剂吸附完全,提高了吸附剂利用率。3)对于高浓度废气,将转速调至高速状态,设备保持为旋转床,吸附剂出口为关闭状态,吸附柱上端加料口也为关闭状态,废气由下至上进入吸附柱进行吸附。After the gas to be treated has been removed and purified, the utility model is used to complete the gas adsorption process, and the appropriate type of adsorption bed is selected according to the concentration of the adsorption medium. Including as follows: 1) For low-concentration exhaust gas, turn off the motor, keep the equipment in fixed bed mode, the adsorption column is filled with adsorbent, the adsorbent is in a static state, and the gas to be treated enters the adsorption column from bottom to top for adsorption; 2) For high Concentrated waste gas, adjust the speed to low speed, keep the equipment in the moving bed mode, the waste gas to be treated is passed into the bed, the adsorbent slowly passes through the adsorption column from top to bottom, and contacts with the gas from bottom to top in countercurrent to complete the adsorption process. During the whole process, fresh adsorbent is continuously added from the upper feeding port, and the adsorbed adsorbent is thrown out from both sides of the adsorption column, and flows into the adsorbent collection port by the spiral plate. The countercurrent contact between the adsorbent and the exhaust gas greatly increases the contact area, so that the gas and the adsorbent are completely adsorbed, and the utilization rate of the adsorbent is improved. 3) For high-concentration exhaust gas, adjust the speed to high speed, keep the equipment as a rotating bed, the outlet of the adsorbent is closed, and the feeding port at the upper end of the adsorption column is also closed, and the exhaust gas enters the adsorption column from bottom to top for adsorption.

本实用新型完成的脱附过程,将吸附饱和的吸附剂装在吸附柱中,封闭吸附剂出口,吸附柱上方加料口封住,调节下方电机,让吸附柱保持在高速状态下旋转,保持旋转床模式,在底部进气口通入水蒸气/热空气,完成脱附过程。整个吸附床在高速状态下旋转,此时为旋转吸附床,在稳定、强大的超重力环境下,吹脱气与吸附剂逆流接触,增强了传质过程,提高了脱附效果,与此同时,本实用新型所述设备大大减小了脱附时间,及时为吸附过程提供新鲜的吸附剂。实验表明,在小试设备中,热空气流量为2.5 m3/h,转速为400 r/min,脱附时间15min,饱和吸附剂便可以达到新鲜吸附剂程度。In the desorption process completed by the utility model, the adsorbent saturated with adsorption is installed in the adsorption column, the outlet of the adsorbent is closed, the feeding port above the adsorption column is sealed, and the lower motor is adjusted to keep the adsorption column rotating at a high speed. In bed mode, water vapor/hot air is fed into the bottom air inlet to complete the desorption process. The entire adsorption bed rotates at a high speed. At this time, it is a rotating adsorption bed. Under a stable and strong supergravity environment, the degassing and degassing contact with the adsorbent in countercurrent, which enhances the mass transfer process and improves the desorption effect. At the same time , The equipment described in the utility model greatly reduces the desorption time, and provides fresh adsorbent for the adsorption process in time. Experiments show that in the small test equipment, the hot air flow rate is 2.5 m 3 /h, the rotation speed is 400 r/min, and the desorption time is 15 minutes, the saturated adsorbent can reach the level of fresh adsorbent.

本实用新型的处理对象一般为常规有机气体,如氯仿、二氯甲烷、丙酮、硫化氢、甲醛等,也以为为挥发性有机气体,如甲苯、二甲苯、甲醛等,也可以为一些易于吸附的工业废气及生活中恶臭气体。所述的吸附剂为固体颗粒物,如活性炭、活性氧化铝、硅胶、分子筛等。所述的吹脱气可以是水蒸气、热空气、氮气等。所述移动吸附床电机的转速为0-50r/min,所述的旋转脱附床电机的转速为100-500r/min。The processing objects of the utility model are generally conventional organic gases, such as chloroform, dichloromethane, acetone, hydrogen sulfide, formaldehyde, etc., also considered as volatile organic gases, such as toluene, xylene, formaldehyde, etc. Industrial waste gas and odorous gas in life. The adsorbent is solid particles, such as activated carbon, activated alumina, silica gel, molecular sieve, etc. The stripping gas can be steam, hot air, nitrogen, etc. The rotational speed of the moving adsorption bed motor is 0-50r/min, and the rotational speed of the rotary desorption bed motor is 100-500r/min.

如图1、图2所示,一种超重力移动吸附床吸附气体设备,包括吸附床主体(固定床、移动床和旋转床一体化),用于固体吸附剂吸附气体,在一套装置中完成吸附、脱附过程。整个设备底部配备电机,底部电机10与上方吸附柱间设有气封装置3,避免由下方进入的有毒、易臭气体泄漏于空气中。吸附柱底部设置气体进口,气体进口可以共用一处,气体进口也设置两处,包括吹脱气进口和废气进口,一个进口使用,另一个进口封闭。废气通过废气进口2进入吸附柱6后,经过气体分布器5,废气体与吸附剂在吸附柱内完成吸附过程,整个吸附过程在密闭状态下进行。吸附剂由吸附剂出口4流出,通过螺旋板8流入吸附剂收集口9处,吸附剂收集口处有回收槽。脱附过程中,吹脱气由吹脱气进口1由下至上通过饱和吸附剂,整个吸附过程也在密闭状态下进行。。整个吸附、脱附过程中可调节电机频率,改变吸附柱转速,进而改变吸附床类型,选择合适吸附床进行吸附、脱附。As shown in Figure 1 and Figure 2, a high-gravity mobile adsorption bed adsorption gas equipment, including the main body of the adsorption bed (fixed bed, moving bed and rotating bed integrated), used for solid adsorbent adsorption gas, in a set of devices Complete the process of adsorption and desorption. The bottom of the whole device is equipped with a motor, and an air seal device 3 is provided between the bottom motor 10 and the upper adsorption column to prevent the poisonous and odorous gas entering from the bottom from leaking into the air. There is a gas inlet at the bottom of the adsorption column. The gas inlet can share one place, and there are also two gas inlets, including the degassing inlet and the waste gas inlet. One inlet is used and the other is closed. After the exhaust gas enters the adsorption column 6 through the exhaust gas inlet 2, it passes through the gas distributor 5, and the exhaust gas and the adsorbent complete the adsorption process in the adsorption column, and the entire adsorption process is carried out in a closed state. The adsorbent flows out from the adsorbent outlet 4, and flows into the adsorbent collection port 9 through the spiral plate 8, and there is a recovery tank at the adsorbent collection port. During the desorption process, the stripping gas passes through the saturated adsorbent from bottom to top through the stripping gas inlet 1, and the entire adsorption process is also carried out in a closed state. . During the whole adsorption and desorption process, the frequency of the motor can be adjusted, the rotation speed of the adsorption column can be changed, and then the type of the adsorption bed can be changed, and the appropriate adsorption bed can be selected for adsorption and desorption.

所述超重力移动吸附床,吸附柱底部进气处设有气体分布器,气体分布器根据实际需求,其为圆锥形设计,设计有夹角为60°、90°、120°三种类型,根据吸附剂颗粒大小选择,气体分布器板面冲有直径小于吸附剂的气体通孔,保证气体可以进入吸附柱,吸附剂不至于跌落。据需求选择不同的圆锥顶角角度和微孔的大小。The supergravity mobile adsorption bed is equipped with a gas distributor at the inlet at the bottom of the adsorption column. The gas distributor is designed in a conical shape according to actual needs, and there are three types of designs with included angles of 60°, 90° and 120°. According to the size of the adsorbent particles, the gas distributor plate is punched with gas through holes with a diameter smaller than that of the adsorbent to ensure that the gas can enter the adsorption column and the adsorbent will not fall. Choose different cone angles and micropore sizes according to your needs.

实施例1:针对气体发生器产生的甲苯气体,采用活性炭作为吸附剂,超重力移动吸附床作为吸附设备进行吸附试验。整个装置的设计处理量为0-15m3/h,吸附柱的直径为50mm,吸附柱的转速可在0-900r/min调节。气体发生器产生的甲苯气体的浓度维持在2000-3000ppm,进气量为5m3/h,实验过程中,通过调节转速,对三种吸附床的吸附性能进行研究,调节吸附柱的转速分别为0r/min、50r/min、500r/min,对应吸附床的模式为固定床、移动床和旋转床。Example 1: For the toluene gas generated by the gas generator, activated carbon was used as the adsorbent, and the high-gravity moving adsorption bed was used as the adsorption equipment to conduct an adsorption test. The designed processing capacity of the whole device is 0-15m 3 /h, the diameter of the adsorption column is 50mm, and the rotation speed of the adsorption column can be adjusted from 0-900r/min. The concentration of toluene gas produced by the gas generator is maintained at 2000-3000ppm, and the intake air volume is 5m 3 /h. During the experiment, the adsorption performance of the three adsorption beds is studied by adjusting the rotation speed. The rotation speed of the adsorption column is adjusted as follows: 0r/min, 50r/min, 500r/min, the corresponding adsorption bed mode is fixed bed, moving bed and rotating bed.

试验过程中,活性炭的装填量为300g,吸附时间为10 h。结果显示,固定床的吸附量为350mg/g,移动床的吸附量为450mg/g,旋转床的吸附量476.8mg/g。During the test, the loading amount of activated carbon was 300 g, and the adsorption time was 10 h. The results showed that the adsorption capacity of the fixed bed was 350 mg/g, that of the moving bed was 450 mg/g, and that of the rotating bed was 476.8 mg/g.

实施例2:对于吸附饱和的活性炭,采用超重力移动吸附床进行脱附,脱附介质为80℃氮气,出口浓度维持在100ppm时,固定床所需的脱附时间为200min,移动床所需的脱附时间为140min,旋转所需的脱附时间为50min;同时测定了,脱附时间为30min,固定床的脱附率为23%,移动床脱附率为36%,旋转床的脱附率为76%,说明旋转床在饱和活性炭脱附方面有较优越的性能。Example 2: For the activated carbon with saturated adsorption, the supergravity moving adsorption bed is used for desorption, the desorption medium is nitrogen at 80 ° C, and when the outlet concentration is maintained at 100 ppm, the desorption time required for the fixed bed is 200 minutes, and the required desorption time for the moving bed is 200 minutes. The desorption time is 140min, and the desorption time required for rotation is 50min; measured simultaneously, the desorption time is 30min, the desorption rate of the fixed bed is 23%, the desorption rate of the moving bed is 36%, and the desorption rate of the rotating bed is 30min. The adsorption rate was 76%, indicating that the rotating bed has superior performance in the desorption of saturated activated carbon.

实施例3:针对浓度为1000ppm的甲苯气体,采用超重力移动吸附床进行吸附、脱附实验。调节转速为0r/min,整个吸附床处于固定床模式,通过气体进口通入10m3/h的甲苯气体,吸附柱中活性炭装填量为500g,吸附10h后,停止通入甲苯气体,换为80%的氮气,调节转速为500r/min,此时吸附床为旋转床模式,进行脱附实验,脱附50min后,在重复前面吸附甲苯气体试验,吸附8h,吸附量达到470mg/g,活性炭仍保持较优的吸附效果,说明超重力移动吸附床再进行吸附、脱附一体化时,保持良好的吸附、脱附效果。Example 3: For toluene gas with a concentration of 1000ppm, adsorption and desorption experiments were carried out by using a high-gravity moving adsorption bed. Adjust the rotating speed to 0r/min, and the whole adsorption bed is in the fixed bed mode. 10m 3 /h of toluene gas is introduced through the gas inlet, and the loading capacity of activated carbon in the adsorption column is 500g. % nitrogen, adjust the rotation speed to 500r/min, and the adsorption bed is in the rotating bed mode at this time, and the desorption experiment is carried out. After desorption for 50 minutes, the previous adsorption toluene gas test is repeated for 8 hours, and the adsorption capacity reaches 470mg/g. Maintaining a better adsorption effect shows that the high-gravity mobile adsorption bed can maintain a good adsorption and desorption effect when the adsorption and desorption are integrated.

Claims (8)

1.一种超重力移动吸附床吸附气体设备,其特征在于所述设备有三种模式,包括固定床模式、移动床模式和旋转床模式,所述设备包括吸附柱,吸附柱中装有吸附剂,通过改变吸附剂在吸附柱中的流速和吸附柱的转速来改变设备的模式。1. A high-gravity moving adsorption bed adsorption gas equipment is characterized in that the equipment has three modes, including fixed bed mode, moving bed mode and rotating bed mode, and the equipment includes an adsorption column, and adsorbent is housed in the adsorption column , by changing the flow rate of the adsorbent in the adsorption column and the rotation speed of the adsorption column to change the mode of the equipment. 2.根据权利要求1所述的超重力移动吸附床吸附气体设备,其特征在于所述吸附柱轴向连接电机,吸附柱底部有进气口、还有吸附剂出口,吸附柱顶部有加料口,所述固定床模式,电机关闭,吸附剂封闭在吸附柱内;所述移动床模式,电机低速转动、吸附剂出口打开、顶部加料口填加吸附剂,吸附剂在吸附柱内自上而下流动;所述旋转床模式,电机高速转动、吸附剂封闭在吸附柱内。2. The high-gravity mobile adsorption bed adsorption gas equipment according to claim 1, characterized in that the adsorption column is axially connected to a motor, the bottom of the adsorption column has an air inlet and an adsorbent outlet, and the top of the adsorption column has a feeding port , in the fixed bed mode, the motor is turned off, and the adsorbent is enclosed in the adsorption column; in the moving bed mode, the motor rotates at a low speed, the adsorbent outlet is opened, and the top feeding port is filled with adsorbent, and the adsorbent flows from top to bottom in the adsorption column In the rotating bed mode, the motor rotates at high speed and the adsorbent is enclosed in the adsorption column. 3.根据权利要求1所述的超重力移动吸附床吸附气体设备,其特征在于所述设备底部设有吸附剂收集口,吸附柱底部的吸附剂出口至吸附剂收集口,由螺旋板顺式下滑,整个吸附和回收过程处在密封环境中。3. The high-gravity mobile adsorption bed adsorption gas equipment according to claim 1, characterized in that the bottom of the equipment is provided with an adsorbent collection port, the adsorbent outlet at the bottom of the adsorption column is connected to the adsorbent collection port, and the spiral plate is cis Sliding down, the entire adsorption and recovery process is in a sealed environment. 4.根据权利要求1所述的超重力移动吸附床吸附气体设备,其特征在于所述吸附柱底部装有气体分布器,气体经气体分布器进入吸附柱内部,其所述的气体分布器为圆锥形设计,锥面上设有微孔,所述的气体分布器与吸附柱同轴线。4. The high-gravity mobile adsorption bed adsorption gas equipment according to claim 1, characterized in that a gas distributor is installed at the bottom of the adsorption column, and the gas enters the interior of the adsorption column through the gas distributor, and the gas distributor is Conical design, with micropores on the conical surface, the gas distributor is coaxial with the adsorption column. 5.根据权利要求1所述的超重力移动吸附床吸附气体设备,其特征在于所述的吸附剂出口与吸附柱轴线呈角度设置,吸附剂出口位于气体分布器上方,吸附剂出口处设置有调节阀。5. The high-gravity mobile adsorption bed adsorption gas equipment according to claim 1, characterized in that the outlet of the adsorbent is set at an angle to the axis of the adsorption column, the outlet of the adsorbent is located above the gas distributor, and the outlet of the adsorbent is provided with regulator valve. 6.根据权利要求1所述的超重力移动吸附床吸附气体设备,其特征在于所述的所述的设备两台串联使用,吸附、脱附连续化运行;其中一台完成吸附过程后,直接通入吹脱气,调高转速,直接进行脱附过程,同时另一台进行吸附过程。6. The high-gravity mobile adsorption bed adsorption gas equipment according to claim 1, characterized in that two of the described equipment are used in series, and the adsorption and desorption are continuously operated; after one of them completes the adsorption process, it is directly Introduce blowing and degassing, increase the speed, and directly carry out the desorption process, while the other one is carrying out the adsorption process. 7.根据权利要求1所述的超重力移动吸附床吸附气体设备,其特征在于所述移动床模式下电机转速为0-50r/min,所述旋转床模式下电机转速为100-500r/min。7. The high-gravity moving adsorption bed adsorption gas equipment according to claim 1, characterized in that the motor speed in the moving bed mode is 0-50r/min, and the motor speed in the rotating bed mode is 100-500r/min . 8.根据权利要求2所述的超重力移动吸附床吸附气体设备,其特征在于所述的进气口包括吹脱气进口和废气进口。8. The high-gravity moving adsorption bed gas adsorption equipment according to claim 2, characterized in that the air inlet includes a stripping gas inlet and a waste gas inlet.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108404601A (en) * 2018-03-30 2018-08-17 中北大学 Hypergravity moves adsorbent bed adsorbed gas equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108404601A (en) * 2018-03-30 2018-08-17 中北大学 Hypergravity moves adsorbent bed adsorbed gas equipment
CN108404601B (en) * 2018-03-30 2024-02-06 中北大学 Gas adsorption equipment of super-gravity movable adsorption bed

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