WO2015055119A1 - 一种新型无源的超重力旋转床装置 - Google Patents

一种新型无源的超重力旋转床装置 Download PDF

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WO2015055119A1
WO2015055119A1 PCT/CN2014/088635 CN2014088635W WO2015055119A1 WO 2015055119 A1 WO2015055119 A1 WO 2015055119A1 CN 2014088635 W CN2014088635 W CN 2014088635W WO 2015055119 A1 WO2015055119 A1 WO 2015055119A1
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rotor
liquid
gas
rotating bed
bed apparatus
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PCT/CN2014/088635
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English (en)
French (fr)
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陈建峰
初广文
鱼潇
赵宏
罗勇
邹海魁
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北京化工大学
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/30—Fractionating columns with movable parts or in which centrifugal movement is caused
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/28—Moving reactors, e.g. rotary drums
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • B01D45/14—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by rotating vanes, discs, drums or brushes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/14—Packed scrubbers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/16—Apparatus having rotary means, other than rotatable nozzles, for atomising the cleaning liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/48—Sulfur compounds
    • B01D53/50—Sulfur oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/48—Sulfur compounds
    • B01D53/52—Hydrogen sulfide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/62—Carbon oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77—Liquid phase processes
    • B01D53/78—Liquid phase processes with gas-liquid contact
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05—Stirrers
    • B01F27/07—Stirrers characterised by their mounting on the shaft
    • B01F27/072—Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis
    • B01F27/0722—Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis perpendicular with respect to the rotating axis
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B01J19/0066—Stirrers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/1806—Stationary reactors having moving elements inside resulting in a turbulent flow of the reactants, such as in centrifugal-type reactors, or having a high Reynolds-number
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00274—Sequential or parallel reactions; Apparatus and devices for combinatorial chemistry or for making arrays; Chemical library technology
    • B01J2219/00277—Apparatus
    • B01J2219/00279—Features relating to reactor vessels
    • B01J2219/00281—Individual reactor vessels

Definitions

  • the invention relates to a novel passive super-gravity rotating bed device, in particular to driving a rotor rotation by a pressure difference of a high-pressure fluid, without using a new super-gravity device driven by a motor, and is suitable for processes of reaction, separation, mixing, etc. of multi-phase flow , belongs to the field of supergravity technology.
  • the British Imperial Chemical Company first proposed the concept of supergravity, and in this concept constructed a supergravity device - a rotating packed bed.
  • the rotating packed bed is powered by a motor, which drives the rotor to rotate at a high speed, which generates a huge centrifugal force.
  • the centrifugal force is used to simulate the super-gravity environment, and the effect of overcoming the gravitational field on the earth is enhanced to strengthen the separation process.
  • Professor Ramshaw of the British Imperial Chemical Company used the supergravity rotating bed for the separation process of rectification for the first time.
  • Professor Chen Jianfeng from Beijing University of Chemical Technology in China used a supergravity rotating bed as a reactor for the reaction process of nanomaterial preparation.
  • the rotational power of a conventional supergravity packed bed rotor comes from the motor drive, which consumes electrical energy.
  • the novel passive supergravity rotating bed provided by the invention does not need to use a motor, and utilizes the flow performance of the high pressure fluid to drive the rotor to rotate, which can effectively save energy and thereby reduce the energy consumption of the entire device. .
  • the first technical problem to be solved by the present invention is to provide a novel passive supergravity rotating bed pack. Set.
  • a second technical problem to be solved by the present invention is to provide an application of the above apparatus in the process of reaction, separation, mixing, etc. of multiphase flow.
  • the present invention provides a novel passive supergravity rotating bed device comprising a casing, a rotor, a rotating shaft, a gas line 1, a gas line 2, a liquid distributor and a liquid outlet;
  • the rotor is disposed in a housing, and the rotor is rotatably connected to the housing through a rotating shaft; the gas line 1, the gas line 2 and the liquid outlet are disposed on the housing; and the liquid distributor is disposed at an inner edge of the rotor The inner edge, the outer edge or the inner and outer edges of the rotor are provided with blades.
  • the passive supergravity rotating bed apparatus of the present invention uses the pressure difference of the high pressure fluid to drive the rotor to rotate without motor drive.
  • a gas line 1 is disposed on the outer casing of the outer rim of the rotor, and a gas entering direction of the gas line 1 faces a side surface of the outer rim of the rotor facing the rotor; To the middle of the rotor cavity.
  • the liquid distributor liquid ejection direction is based on the principle of facilitating the rotation of the blade, preferably perpendicular to the form of the blade, to maximize the rotation of the blade.
  • the blades may be curved blades and straight blades. More preferably, the vanes are at least two, evenly disposed on the inner, outer or inner and outer edges of the rotor.
  • the housing is provided with a groove, and a bearing is arranged in the groove, and the rotating shaft is fixed in the bearing.
  • the entire rotating shaft is fixed in the housing, and there is no need to seal between the shaft and the outer casing, which can reduce the cost of the equipment.
  • the rotating shaft is installed in a vertical or horizontal manner.
  • the rotor is a packed rotor or a non-filled rotor. Make a choice based on process requirements.
  • the present invention provides an application of the above apparatus in the operation of reaction, separation, mixing, etc. of a multiphase flow, wherein the multiphase flow includes a high pressure fluid.
  • the powerful pressure difference generated by the fluid is used to drive the rotor to achieve energy saving.
  • the pressure is ⁇ 500 Pa.
  • the high pressure fluid includes, but is not limited to, a gas, a liquid or a supercritical fluid, and the like.
  • the multiphase flow includes, but is not limited to, gas liquid, liquid liquid, gas solid, gas liquid solid, and the like.
  • the multi-phase flow operation process in the passive supergravity rotating bed device of the present invention may be a countercurrent, cocurrent or cross-flow operation; suitable for various flow forms, and has a wide range of applications.
  • the high pressure fluid can drive the rotor from the outer cavity, the inner cavity or the inner and outer cavity of the rotor to drive the rotor Rotating to meet the requirements of omitting the motor and greatly reducing energy consumption.
  • the device of the invention is more energy-saving and more compact in structure, and can eliminate the rotary seal connected to the shaft and the shell, and the utility model has the low cost. Since the rotating parts are all enclosed in the casing, the safety performance of the device is further improved, and it can be easily used for high temperature and high pressure reaction, absorption and the like.
  • FIG. 1 is a schematic view showing the structure of a vertical new passive supergravity rotating bed of the present invention
  • Figure 2 is a cross-sectional view of the vertical new passive supergravity rotating bed of the present invention
  • FIG. 3 is a schematic structural view of a horizontal type new passive supergravity rotating bed of the present invention.
  • Figure 5 is a flow chart of the parallel flow absorption process of the vertical novel passive supergravity rotating bed of the present invention.
  • a passive supergravity rotating bed apparatus includes a housing 1, a rotor 3, a rotating shaft 8, a gas line 1-2, a gas line 2, a liquid distributor 5, and a liquid outlet. 7; the liquid outlet 7 is disposed at a lower portion of the casing 1; the rotor 3 is disposed in the casing 1, and a sealing device 6 is disposed between the rotor 3 and the casing 1 so that both the incoming gas and the liquid need to pass through the rotor
  • the bottom of the casing 1 is provided with a groove, and a bearing 9 is arranged in the groove.
  • the rotating shaft 8 is fixed in the bearing 9, that is, the rotating shaft 8 is arranged vertically; thus, the entire rotating shaft 8 is fixed to the casing.
  • the inner edge of the rotor 3 is provided with a rotor inner edge blade 10
  • the outer edge of the rotor 3 is provided with a rotor outer edge blade 11
  • a gas line 2 is disposed on the outer casing 1 of the rotor outer edge blade 11, and the gas inlet direction 15 of the gas pipe 2 faces the one side surface of the rotor outer edge blade 11 toward the rotor 3 (see the figure).
  • the second 4 opens to the central cavity of the rotor 3; the liquid distributor 5 is disposed at the inner edge of the rotor 3; the passive supergravity rotating bed apparatus of the present invention drives the rotor by the pressure difference of the high pressure fluid (gas or/and liquid) Rotating, no motor drive;
  • the liquid distributor 5 liquid ejection direction 14 is perpendicular to the rotor inner edge blade 10 (see FIG. 2), and the rotation of the rotor inner edge blade is maximized;
  • the rotor outer edge blade 11 is a curved blade, the rotor outer edge blade 11 is provided with twelve, uniformly disposed on the outer edge of the rotor; the rotor inner edge blade 10 is a curved blade, and the rotor inner edge blade 10 is There are 8 pieces, which are evenly arranged on the outer edge of the rotor.
  • Example 1 is repeated except that the rotating shaft 8 is disposed horizontally within the housing 1.
  • FIGS. 4 Shown, see FIGS. 4 to absorb high pressure natural gas CO.'S Example 2; using the CO 2 content of 10% by high pressure natural gas, from a gas line 2 enters, the outer edge of the rotor drive blades 11, rotation of the drive rotor; 40wt% of liquid absorbent
  • the MDEA enters the liquid distributor 5 from the liquid inlet, and the gas-liquid countercurrent contact completes the mass transfer process, the liquid flows out of the liquid outlet 7, and the gas flows out from the gas line 2 .
  • the CO 2 content was 2.5%.

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  • Environmental & Geological Engineering (AREA)
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  • Biomedical Technology (AREA)
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Abstract

一种无源的超重力旋转床装置，包括壳体（1）、转子（3）、旋转轴（8）、气体管路一（2）、气体管路二（4）、液体分布器（5）和液体出口（7）；转子（3）设置在壳体（1）内，转子（3）通过旋转轴（8）与壳体（1）旋转连接；气体管路一（2）、气体管路二（4）和液体出口（7）设置在壳体（1）上；液体分布器（5）设置在转子（3）的内缘处；转子（3）的内缘、外缘或内外缘设有叶片（10,11），高压流体驱动叶片（10,11）带动转子（3）旋转，无电机驱动。

Description

一种新型无源的超重力旋转床装置 技术领域
本发明涉及一种新型无源的超重力旋转床装置，具体涉及用高压流体的压差驱动转子旋转，无需使用电机驱动的新型超重力装置，适用于多相流的反应、分离、混合等过程，属于超重力技术领域。
背景技术
19世纪70年代，英国帝国化学公司首次提出了超重力的概念，并在此概念上构造了超重力设备——旋转填充床。旋转填充床以电机为动力，带动转子高速旋转，从而产生巨大的离心力，用离心力来模拟超重力环境，实现了在地球上克服重力场的作用来强化分离过程。1983年，英国帝国化学公司Ramshaw教授首次将超重力旋转床用于精馏的分离过程。1995年，中国北京化工大学陈建峰教授将超重力旋转床作为反应器，用于纳米材料制备的反应过程中，从此开启了超重力旋转床反应器工程与应用的研究。目前，以超重力旋转床作为设备载体的超重力技术已经成功的解决了多个化工过程难题，在尾气SO2脱除、烟气CO2捕集、精馏、纳米材料制备、废水处理、聚合物脱挥等多个领域实现了工业应用。
2006年，全国累计探明的天然气可开采量为3.84万亿立方。在天然气开采过程中，由于天然气密度小，为0.75～0.8kg/m3，井筒气柱对井底的压力小；天然气粘度小，在地层和管道中的流动阻力也小；又由于膨胀系数大，其弹性能量也大。因此天然气开采时一般采用自喷方式,天然气在气井自身的压力下，从井底连续举升到地面，因此采出到地面的天然气本身带有一定的压力。类似于蒸汽发电，带压的天然气在后续处理过程中如果能利用其压力做功，则能大大节约能量。
然而，传统超重力填充床转子的旋转动力来自电机驱动，电机驱动消耗电能。为响应我国节能减排的政策要求，本发明提供的新型无源的超重力旋转床无需使用电机，利用高压流体自身的流动性能带动转子转动，能有效的节约能量，进而降低整个装置的能量消耗。
发明内容
本发明要解决的第一个技术问题是提供一种新型无源的超重力旋转床装 置。
本发明要解决的第二个技术问题是提供上述装置在多相流的反应、分离、混合等操作过程中的应用。
为解决上述第一个技术问题，本发明一种新型无源的超重力旋转床装置，包括壳体、转子、旋转轴、气体管路一、气体管路二、液体分布器和液体出口；所述转子设置在壳体内，该转子通过旋转轴与壳体旋转连接；所述气体管路一、气体管路二和液体出口设置在壳体上；所述液体分布器设置在转子的内缘处；所述转子的内缘、外缘或内外缘设有叶片。本发明无源的超重力旋转床装置利用高压流体的压差驱动转子旋转，无电机驱动。
优选地，所述转子外缘叶片外的壳体上设置气体管路一，所述气体管路一的气体进入方向正对转子外缘叶片朝向转子的一侧表面；所述气体管路二通向转子中部空腔。
优选地，所述液体分布器液体喷射方向以有利于推动叶片旋转的角度为原则，优选垂直于叶片的形式，最大程度的带动叶片旋转。
优选地，所述叶片可以是弯曲叶片和直叶片。更优选地，所述叶片至少两个，均匀地设置在转子内缘、外缘或内外缘。
优选地，所述壳体上设有凹槽，凹槽内设有轴承，所述旋转轴固定在轴承内。这样，整个旋转轴固定在壳体内，轴与外壳之间不需要进行密封，可以减少设备造价。
优选地，所述旋转轴为立式或者卧式安装。
优选地，所述转子为填料式转子或无填料转子。根据工艺要求作出选择。
为解决上述第二个技术问题，本发明一种上述装置在多相流的反应、分离、混合等操作过程中的应用，所述多相流中包括高压流体。利用该类流体产生的强大压差带动转子转动以达到节能的目的。
优选地，压力≥500Pa。
优选地，所述高压流体包括但不限于气体、液体或超临界流体等。
优选地，所述的多相流包括但不限于气液、液液、气固、气液固等。
优选地，本发明无源超重力旋转床装置中多相流操作过程可以是逆流、并流或错流操作；适合多种流动形式，具有广泛的应用领域。
本发明中，高压流体可以从转子外腔、内腔或内外腔驱动叶片带动转子 旋转，从而满足省略电机的要求，大幅的减少能耗。
本发明的有益效果：
本发明装置与传统超重力旋转床相比更加节能、结构更加紧凑，可省去轴与外壳相连的旋转密封，造价低。由于转动部分全部包在壳体内，使设备的安全性能进一步提高，且可轻松用于高温高压的反应、吸收等场合。
附图说明：
图1是本发明的立式新型无源超重力旋转床结构示意图；
图2是本发明的立式新型无源超重力旋转床AA截面图；
图3是本发明的卧式新型无源超重力旋转床结构示意图；
图4是本发明的立式新型无源超重力旋转床逆流吸收工艺流程图；
图5是本发明的立式新型无源超重力旋转床并流吸收工艺流程图；
其中
1-外壳；2-气体管路一；3-转子；4-气体管路二；5-液体分布器；6-密封装置；7-液体出口；8-旋转轴；9-轴承；10-转子内缘叶片；11-转子外缘叶片；12-原料罐；13-泵；14-液体喷射方向；15-气体进入超重力旋转床装置方向。
具体实施方式
下面结合附图和实施例对本发明的实施方案做进一步说明。但本发明不限于所列出的实施例。
实施例1
参见图1、2所示，一种无源的超重力旋转床装置，包括壳体1、转子3、旋转轴8、气体管路一2、气体管路二4、液体分布器5和液体出口7；所述液体出口7设置在壳体1下部；所述转子3设置在壳体1内，且转子3和壳体1之间设有密封装置6，使得进入的气体和液体均需通过转子；所述壳体1底部设有凹槽，凹槽内设有轴承9，所述旋转轴8固定在轴承9内，即旋转轴8为立式设置；这样，整个旋转轴8固定在壳体1内，旋转轴8与外壳1之间不需要进行密封，可以减少设备造价；所述转子3的内缘设有转子内缘叶片10，所述转子3的外缘设有转子外缘叶片11；所述转子外缘叶片11外的壳体1上设置气体管路一2，所述气体管路一2的气体进入方向15正对转子外缘叶片11朝向转子3的一侧表面(参见图2所示)；所述壳体1上的气体管路 二4通向转子3中部空腔；所述液体分布器5设置在转子3的内缘处；本发明无源的超重力旋转床装置利用高压流体(气体或/和液体)的压差驱动转子旋转，无电机驱动；
所述液体分布器5液体喷射方向14垂直于转子内缘叶片10(参见图2所示)，最大程度的带动转子内缘叶片旋转；
所述转子外缘叶片11是弯曲叶片，所述转子外缘叶片11设有12个，均匀地设置在转子外缘上；所述转子内缘叶片10是弯曲叶片，所述转子内缘叶片10设有8个，均匀地设置在转子外缘上。
实施例2
参见图3所示，重复实施例1，其不同仅在于，旋转轴8卧式设置在壳体1内。
实施例3
一种上述实施例1所述装置在多相流的分离过程中的应用：
参见图4所示，以高压天然气CO2吸收为例；利用CO2含量为10％的高压天然气，从气体管路一2进入，驱动转子外缘叶片11，驱动转子旋转；吸收液40wt％的MDEA从液体进口进入液体分布器5，气液逆流接触完成传质过程，液体从液体出口7流出，气体从气体管路二4流出。CO2含量为2.5％。
实施例4
一种上述实施例1所述装置在多相流的吸收过程中的应用：
参见图4所示，以硫酸行业尾气SO2吸收为例；利用SO2含量为6000mg/m3的尾气，从气体管路一2进入；高压的氨液吸收液从原料罐12经泵13输送到无源的超重力旋转床装置的液体进口进入液体分布器5，驱动转子内缘叶片10，驱动转子旋转。气液逆流接触完成传质过程，液体从液体出口7流出，气体从气体管路二4流出；SO2含量为95mg/m3。
实施例5
一种上述实施例1所述装置在多相流的吸收过程中的应用：
参见图4所示，以高压天然气H2S吸收为例；利用H2S含量为2.2％的高压天然气，从气体管路一2进入，驱动转子外缘叶片11，驱动转子旋转。高压的含铁络合吸收液从原料罐12经泵13输送到无源的超重力旋转床装置的液体进口进入液体分布器5，驱动转子内缘叶片10，同向驱动转子旋转。气 液逆流接触完成传质过程，液体从液体出口7流出，气体从气体管路二4流出。H2S含量为0.18％。
实施例6
一种上述实施例1所述装置在多相流的吸收过程中的应用：
参见图5所示，，以炼厂尾气H2S吸收为例；利用H2S含量为2.2％的炼厂尾气，从气体管路二4进入；高压的吸收液含铁络合脱硫剂从原料罐12经泵13输送到无源的超重力旋转床装置的液体进口进入液体分布器5，驱动转子内缘叶片10，驱动转子旋转。气液并流接触完成传质过程，液体从液体出口7流出，气体从气体管路一2流出；H2S含量为0.85％。
显然，本发明的上述实施例仅仅是为清楚地说明本发明所作的举例，而并非是对本发明的实施方式的限定。对于所属领域的普通技术人员来说，在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无法对所有的实施方式予以穷举。凡是属于本发明的技术方案所引伸出的显而易见的变化或变动仍处于本发明的保护范围之列。

Claims (10)

  1. 一种新型无源的超重力旋转床装置，包括壳体、转子、旋转轴、气体管路一、气体管路二、液体分布器和液体出口；所述转子设置在壳体内，该转子通过旋转轴与壳体旋转连接；所述气体管路一、气体管路二和液体出口设置在壳体上；所述液体分布器设置在转子的内缘处；其特征在于：所述转子的内缘、外缘或内外缘设有叶片。
  2. 根据权利要求1所述超重力旋转床装置，其特征在于：优选地，所述转子外缘叶片外的壳体上设置气体管路一，所述气体管路一的气体进入方向正对转子外缘叶片朝向转子的一侧表面；所述气体管路二通向转子中部空腔。
  3. 根据权利要求1所述超重力旋转床装置，其特征在于：优选地，所述液体分布器液体喷射方向垂直于转子内缘叶片。
  4. 根据权利要求1所述超重力旋转床装置，其特征在于：优选地，所述叶片可以是弯曲叶片和直叶片；更优选地，所述叶片至少两个，均匀地设置在转子内缘、外缘或内外缘。
  5. 根据权利要求1所述超重力旋转床装置，其特征在于：优选地，所述壳体上设有凹槽，凹槽内设有轴承，所述旋转轴固定在轴承内。
  6. 根据权利要求1所述超重力旋转床装置，其特征在于：优选地，所述旋转轴为立式或者卧式安装。
  7. 根据权利要求1所述超重力旋转床装置，其特征在于：优选地，所述转子为填料式转子或无填料转子。
  8. 一种上述权利要求1-7中任一超重力旋转床装置在多相流的反应、分离、混合等操作过程中的应用，其特征在于：所述多相流中包括高压流体。
  9. 根据权利要求8所述的应用，其特征在于：优选地，压力≥500Pa。
  10. 根据权利要求8所述的应用，其特征在于：
    优选地，所述高压流体包括气体、液体或超临界流体；
    优选地，所述的多相流包括气液、液液、气固或气液固；
    优选地，多相流操作过程是逆流、并流或错流操作。
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