CN1032120C - 变压吸附程序控制操纵装置 - Google Patents
变压吸附程序控制操纵装置 Download PDFInfo
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- CN1032120C CN1032120C CN91107269A CN91107269A CN1032120C CN 1032120 C CN1032120 C CN 1032120C CN 91107269 A CN91107269 A CN 91107269A CN 91107269 A CN91107269 A CN 91107269A CN 1032120 C CN1032120 C CN 1032120C
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- 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
- B01D53/02—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 by adsorption, e.g. preparative gas chromatography
- B01D53/04—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 by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0454—Controlling adsorption
-
- 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
- B01D53/02—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 by adsorption, e.g. preparative gas chromatography
- B01D53/04—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 by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
- B01D53/0446—Means for feeding or distributing gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40003—Methods relating to valve switching
-
- 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
- B01D53/02—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 by adsorption, e.g. preparative gas chromatography
- B01D53/04—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 by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/047—Pressure swing adsorption
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Control Of Fluid Pressure (AREA)
- Separation Of Gases By Adsorption (AREA)
- Multiple-Way Valves (AREA)
- Mechanically-Actuated Valves (AREA)
- Fluid-Pressure Circuits (AREA)
- Magnetically Actuated Valves (AREA)
- Fluid-Driven Valves (AREA)
Abstract
变压吸附程序控制操纵装置属石油、化工、冶金行业变压吸附气体分离用控制装置,其中程序控制阀采用油压集成驱动机构,程序控制阀的密封比压采用油压、气压控制机构,设置有程序控制阀的开关位置检测机构,并在阀门驱动部分和密封结构上采用新颖设计,使变压吸附装置在稳定性和可靠性方面得到改善。
Description
本发明涉及作业类,特别是用于石油、化工、冶金行业变压吸附法气体分离工艺装置的程序控制和操纵装置。
截止目前,世界各国在变压吸附程序控制上都是广泛使用电动或气动控制装置,由控制机、电气转换部件、气动放大器和气动控制阀构成,存在着密封性差、寿命短等缺点。CN1005611B西德林德股份公司的专利申请公开了一种“变压吸附法及其系统”,主要从工艺方法上优化了变压吸附过程;CN1031660A联合碳化公司申请的专利“变压吸附控制方法和设备”,也仅仅是从精简阀门数量上来提高变压吸附设备运行的可靠性,都未从改变控制设备的动力源、结构和操纵方式上解决设备的密封性及使用寿命等问题。
本发明的目的是针对变压吸附装置已有技术的不足,提供一种变压吸附装置的以压力油为动力源的程序控制操纵装置,解决控制机构的密封和寿命存在的问题,为变压吸附装置的稳定性、可靠性提供保障。
本发明的目的采取以下措施实现,变压吸附程序控制操纵装置包含控制计算机,程序控制阀开关驱动机构和程序控制阀密封控制机构,其特征是程序控制阀采用集成油压开关驱动机构,程序控制阀的密封控制机构采用油压或气压密封比压控制机构,驱动机构的油缸活塞采用分块式结构,并设置有程序阀开关位置检测机构。
本发明与已有技术相比,其优点在于,由于采用了集成油压开关驱动机构,功率大,动作稳定可靠,满足了不同工艺流程的变压吸附系统的要求;程序控制阀采用油压、气压密封比压控制机构以及驱动机构的油缸活塞采用分块式结构,使整体密封性加强,且摩擦磨损降低从而使用寿命增长;阀位检测机构准确检测阀的开关状态信号,反馈到计算机进行判断处理,保障了变压吸附装置的运行可靠性。
附图图面说明如下,现结合实施例叙述:
图1为变压吸附程序控制操纵装置的组成方框图。
图2为变压吸附程序控制操纵装置的集成油压方框图。
图3为变压吸附程序控制操纵装置的程序控制阀结构简图。
图4为变压吸附程序控制操纵装置的程序控制阀开关驱动机构结构简图。
图5为变压吸附程序控制操纵装置的程序控制阀油压、气压密封比压控制机构简图。
由图1,计算机用于控制既定的变压吸附工艺所设定的程序操作,具有输出控制信号、显示工作状态、接收阀位反馈信号、判断工艺状态、报警联锁和处理生产故障,用于这套装置的计算机可选取包括单片机、单板机、工业控制机、通用系统机和集散型计算机系统等。集成油压装置由电-液换向阀、手动阀和集成油路构成,电-液换向阀接收计算机输出的直流或交流电信号,使油路关断或开通,以驱动程序控制阀开关和程序控制阀密封比压控制机构。电-液换向阀可选用标准的24EO-B10H-T,24DO-B10H-T等。程序控制阀的开关采用油压驱动,装有阀位检测机构。程序控制阀除球型阀外,可供选用的还有蝶阀、闸阀、座板阀和旋塞阀等。
由图2,以油压集成块为核心将供油泵、电-液换向阀、压力安全保护阀以及执行部件联系起来。执行部件包含两部分,一部分为程序控制阀的开关驱动部件,另一部分为程序控制阀密封比压控制机构的控制部件。
由图3,程序控制阀开关和密封的协调动作是这样进行:要关闭阀门首先由端盖1与滑动密封环2形成的环形油腔3压力卸荷,密封比压减小,维持一定背压,然后外加的驱动部件使转轴4带动阀芯5转动90°,到位后油腔3的压力加载推动滑动密封环2使密封圈6紧贴于阀芯5,增加密封比压保持密封。要打开阀门,以上4、5的转动反向。
由图4,程序控制阀开关驱动机构由带齿条的活塞杆7使带齿轮的阀芯转轴4转动从而实现程序控制阀的开关驱动。阀外的电磁式位置传感器8从转轴4上的永久电磁铁9的极性获得阀的开关位置信号,再返回计算机处理。程序控制阀开关驱动机构上的油缸活塞采用分块式结构,浮动活塞密封块10的圆周密封均匀,不易受齿条齿轮传动偏载力的影响,从而改善了活塞密封效果。驱动机构还可采用拔叉式驱动、转动缸驱动、油马达驱动等机构。
由图5,程序控制阀密封控制机构,由密封圈6、阀体端盖1、滑动密封环2以及1和2形成的两个功能空腔组成,其中一个空腔作为变载压力油腔3,在压力油作用下推动滑动密封环2使密封圈6紧贴于阀芯5,增大比压保持密封,另一个空腔11与外界相通,成为间隙泄漏通道,避免对工艺系统的污染。
Claims (3)
1、一种变压吸附程序控制操纵装置,包括控制计算机、程序控制阀开关驱动机构、程序控制阀密封控制机构、程序控制阀以及程序控制阀并关位置检测机构,其特征在于:
A、所述程序控制阀采用集成油压开关驱动机构,程序控制阀的密封控制机构采用油压或气压密封比压控制机构,
B、所述程序控制阀密封控制机构由程序控制阀的阀体端盖和滑动密封环构成的用于控制程序控制阀密封比压的功能腔及在阀体端盖与滑动密封环间构成的与外界相通的作为泄漏通道的功能腔和所述集成油压或气压机构所组成,
C、程序控制阀开关位置检测机构由阀外电磁式位置传感器和设置在程序控制阀阀芯转轴上的磁铁组成。
2、根据权利要求1所述的变压吸附程序控制操纵装置,其特征在于:所述程序控制阀开关驱动机构中的油缸的活塞采用分块结构。
3、根据权利要求1所述的变压吸附程序控制操纵装置,其特征在于:所述的程序控制阀密封控制机构是一套气压机构。
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN91107269A CN1032120C (zh) | 1991-08-14 | 1991-08-14 | 变压吸附程序控制操纵装置 |
| US07/923,502 US5240481A (en) | 1991-08-14 | 1992-08-03 | Programmable control and operation equipment of swing pressure adsorption process |
| DE4226827A DE4226827C2 (de) | 1991-08-14 | 1992-08-13 | Programmierbare Steuer- und Betriebsvorrichtung für ein druckwechselbeaufschlagtes Adsorptionsverfahren |
| JP21622492A JP3327582B2 (ja) | 1991-08-14 | 1992-08-13 | スイング圧力吸着プロセスのプログラム可能な制御/操作設備 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN91107269A CN1032120C (zh) | 1991-08-14 | 1991-08-14 | 变压吸附程序控制操纵装置 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1059295A CN1059295A (zh) | 1992-03-11 |
| CN1032120C true CN1032120C (zh) | 1996-06-26 |
Family
ID=4908624
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN91107269A Expired - Lifetime CN1032120C (zh) | 1991-08-14 | 1991-08-14 | 变压吸附程序控制操纵装置 |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US5240481A (zh) |
| JP (1) | JP3327582B2 (zh) |
| CN (1) | CN1032120C (zh) |
| DE (1) | DE4226827C2 (zh) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5591254A (en) * | 1995-07-12 | 1997-01-07 | Jordan Holding Company | Vapor recovery system with automatic valve control |
| US5685896A (en) * | 1996-02-06 | 1997-11-11 | Westinghouse Air Brake Company | Linear choke shuttle/orifice check valve mechanism for a twin tower air dryer |
| WO1997048477A1 (en) * | 1996-06-21 | 1997-12-24 | Jordan Holding Company | Return circuit for vapor recovery system |
| US6409807B1 (en) * | 2000-05-23 | 2002-06-25 | Litton Systems, Inc. | Linear gas valve cycle control, shut-off-valve and self test |
| US6926756B1 (en) * | 2003-03-31 | 2005-08-09 | Macronix International Co. Ltd. | Method and apparatus for controlling the operation of a scrubber |
| GB2460096B (en) * | 2008-06-27 | 2010-04-07 | Wajid Rasheed | Expansion and calliper tool |
| US8979982B2 (en) | 2013-05-01 | 2015-03-17 | Jordan Technologies, Llc | Negative pressure vapor recovery system |
| CN109210031A (zh) * | 2018-09-29 | 2019-01-15 | 宁波诚天液压有限公司 | 一种电磁手动换向阀 |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1887606A (en) * | 1930-03-08 | 1932-11-15 | Mable M Thomas | Air purifier |
| US3160486A (en) * | 1962-04-24 | 1964-12-08 | Gilbert & Barker Mfg Co | Fluid operated timing apparatus |
| US3775946A (en) * | 1972-10-13 | 1973-12-04 | Howe Baker Eng | Adsorption control |
| US3898047A (en) * | 1973-07-17 | 1975-08-05 | Bendix Corp | Oxygen generation system |
| US4101298A (en) * | 1977-04-05 | 1978-07-18 | The Bendix Corporation | Pressure cycling control for fluid separator mechanism |
| CA1100418A (en) * | 1977-07-18 | 1981-05-05 | Leslie W. Sandman | Adsorbent fractionator with effluent powered cycle control and process |
| US4322228A (en) * | 1977-10-06 | 1982-03-30 | The Bendix Corporation | Pneumatically actuated electronic control for a fluid mixture adsorption separator |
| DE2823211A1 (de) * | 1978-05-27 | 1979-12-06 | Bayer Antwerpen Nv | Verfahren zum betrieb einer druck- wechsel-adsorptionsanlage |
| US4247311A (en) * | 1978-10-26 | 1981-01-27 | Pall Corporation | Downflow or upflow adsorbent fractionator flow control system |
| DE2851847A1 (de) * | 1978-11-30 | 1980-06-12 | Linde Ag | Verfahren zum betrieb einer zyklisch arbeitenden druckwechsel-adsorptionsanlage |
| DE3040495C2 (de) * | 1980-10-28 | 1986-10-23 | Linde Ag, 6200 Wiesbaden | Ventilsteuerung |
| US4631073A (en) * | 1984-03-15 | 1986-12-23 | Wilkerson Corporation | Method and apparatus for theadsorptive fractionation of gases |
| US5137549A (en) * | 1988-10-14 | 1992-08-11 | Vbm Corporation | Two stage super-enriched oxygen concentrator |
| US5154737A (en) * | 1990-01-12 | 1992-10-13 | Vbm Corporation | System for eliminating air leakage and high purity oxygen of a PSA oxygen concentrator |
-
1991
- 1991-08-14 CN CN91107269A patent/CN1032120C/zh not_active Expired - Lifetime
-
1992
- 1992-08-03 US US07/923,502 patent/US5240481A/en not_active Expired - Lifetime
- 1992-08-13 JP JP21622492A patent/JP3327582B2/ja not_active Expired - Fee Related
- 1992-08-13 DE DE4226827A patent/DE4226827C2/de not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP3327582B2 (ja) | 2002-09-24 |
| JPH06182132A (ja) | 1994-07-05 |
| US5240481A (en) | 1993-08-31 |
| DE4226827C2 (de) | 2002-05-02 |
| CN1059295A (zh) | 1992-03-11 |
| DE4226827A1 (de) | 1993-02-18 |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C15 | Extension of patent right duration from 15 to 20 years for appl. with date before 31.12.1992 and still valid on 11.12.2001 (patent law change 1993) | ||
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| CX01 | Expiry of patent term |
Expiration termination date: 20110814 Granted publication date: 19960626 |