CN205803007U - A kind of multimode combination type nitrogen production by air separation oxygenerator - Google Patents
A kind of multimode combination type nitrogen production by air separation oxygenerator Download PDFInfo
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- CN205803007U CN205803007U CN201620226267.7U CN201620226267U CN205803007U CN 205803007 U CN205803007 U CN 205803007U CN 201620226267 U CN201620226267 U CN 201620226267U CN 205803007 U CN205803007 U CN 205803007U
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Abstract
A kind of multimode combination type nitrogen production by air separation oxygenerator is collectively constituted by adsorption tower module or membrance separation module, valve pipeline module, deafener module, process tank module, electronic control module and Pneumatic module, and intermodule can use the various ways such as flange, snap joint, screw thread, flexible pipe to connect.Adsorption tower module is made up of several adsorption towers and chassis, and adsorption tower module can be formed absorption tower system by Liang Ta, three towers, four towers and multitower, but each adsorption tower module is at least made up of two adsorption towers alternately.Each module can realize the production of standard component; intermodule can freely assemble; save processing cost; improve device maintainability and parts interchangeability; realize unit scale metaplasia to produce, it is ensured that the quality of production, reduce production cost, maintenance cost, logistics cost; shorten the process-cycle, meet the market demand.
Description
Technical field
This utility model belongs to pressure-variable adsorption and membrance separation space division field, it is adaptable to nitrogen production by air separation and making oxygen by air separation field,
It is specifically related to a kind of multimode combination type nitrogen production by air separation oxygenerator.
Background technology
Existing nitrogen production by air separation, oxygenerator are typically by adsorption tower or film bucket, chassis, air inlet pipeline, outlet pipe, aerofluxus
Pipeline, automatically controlled instrument, air intake valve, valve of giving vent to anger, drain tap, various manually-operated gate and deafener etc. form.Valve is installed
After the pipeline of door and adsorption tower form a whole, it is commonly mounted on chassis, and automatically controlled instrument and deafener depend on pipeline
Carry out installing with chassis and fix.The equipment of this globality is highly detrimental to the replacing of equipment maintenance and parts.At present
On market nitrogen oxygenerator processed be typically all require to be designed according to user, processing, be substantially non-standard equipment, every
Equipment all obtain individually designed, individually process, it is impossible to accomplishing scale production, the quality of production is difficult to ensure that, and production cost, maintenance
Expense, logistics cost are high, and the process-cycle is long.
Summary of the invention
In order to solve the problems referred to above, this utility model provides a kind of multimode combination type nitrogen production by air separation oxygenerator, suitable
For nitrogen production by air separation field and making oxygen by air separation field.This utility model be the technical scheme is that a kind of multimode combination type
Nitrogen production by air separation oxygenerator by adsorption tower module or membrance separation module, valve pipeline module, deafener module, process tank module,
Electronic control module and Pneumatic module collectively constitute, and intermodule can use the various ways such as flange, snap joint, screw thread, flexible pipe to connect.
Each module can realize the production of standard component, and intermodule can freely assemble, and reduces welding quantity, saves processing cost, carry
High device maintainability and parts interchangeability.Nitrogen oxygenerator processed in this utility model, when nitrogen quantity processed or oxygen making amount not
Simultaneously, it is not necessary to redesign or strengthen the volume of adsorption tower or change global design, and having only to correspondingly increase adsorption tower
Group or the quantity of membrane module.Such as, when nitrogen oxygen making amount processed is beyond the load of an absorption tower system, can multiple suctions in parallel
Attached tower system or membrane module, therefore have only to the gas production according to matching requirements, and each absorption tower system or the product nitrogen of membrane module
Producing oxygen ability, absorption tower system or the membrane module of opening respective number carry out parallel operation, it is achieved that apparatus module
The first step.
Adsorption tower module is made up of several adsorption towers and chassis, and adsorption tower module can be by Liang Ta, three towers, four towers and multitower
Composition absorption tower system, but each adsorption tower module is at least made up of two adsorption towers alternately.Nitrogen oxygenerator processed according to
Product tolerance purity selects one or more absorption tower system, and adsorption tower is divided into several model, ting model adsorption tower to be suitable for little tolerance
Equipment, when gas production requires bigger, should select relatively large adsorption tower composition absorption tower system.The adsorption tower of every kind of model all can realize
Mass production, reduces and manufactures and designs and logistics transportation cost, and then realizes the standardization of nitrogen oxygenerator processed, scale metaplasia
Produce.
Membrance separation module is collectively constituted by one or more film bucket, related film assembly and chassis or support.
Valve pipeline module is by intake valve, air outlet valve, air bleeding valve, equalizing valve and admission line, outlet pipe, exhaustor
Road, pressure-equalizing passageway and corresponding manual auxiliary valve and pipeline composition, the valve in valve pipeline module can be by electromagnetic valve, pneumatic
Or electric angle seat valve, pneumatically or electrically stop valve, pneumatically or electrically butterfly valve and corresponding manual ball valve, needle-valve, gate valve, cut-off
Valve, butterfly valve form.
Deafener module is made up of one or more deafeners, and muffler entrance is aggregated in a total air escape pipe road, disappears
Sound device module can additional silencer cover, also can be not added with silencer cover, also can cause equipment storeroom remotely or outdoor.
Electronic control module is such as switched electricity by Programmable Logic Controller, gas analyser, touch screen, electromagnetic valve and some electric adjuvants
Source, binding post, chopper, insurance etc. form, and whole automatically controlled part is divided into again four little modules: Programmable Logic Controller module,
Gas analyser module, power module, terminal module.Arbitrary module goes wrong, and can individually be extractd by problem module, changes
Spare parts, convenience easy to maintenance, failture evacuation is rapid.
Pneumatic module is made up of some gladhands, flexible pipe, fixed support or casing, including some inlet suction ports and
Some air outlet adapters form, and inlet suction port connects the electromagnetic valve gas outlet in electronic control module, and air outlet adapter connects in valve pipe module
Pneumatic valve head pilot 3-port transfer.Pneumatic module can make box, folded plate type, plate armature.If valve module does not uses
Operated pneumatic valve, then in this nitrogen oxygenerator processed, Pneumatic module can omit.
Accompanying drawing explanation
Fig. 1 is for adsorbing tower multimode combination type nitrogen production by air separation oxygenerator schematic diagram.
In figure, 1. deafener module；2. adsorption tower module；3. process tank module；4. electronic control module；5. Pneumatic module；6.
Valve pipeline module.
Fig. 2 is membrance separation formula multimode combination type nitrogen production by air separation oxygenerator schematic diagram.
In figure, 1. deafener module；2. valve pipeline module；3. membrance separation module；4. electronic control module；5. Pneumatic module.
Specific embodiment
Below in conjunction with the accompanying drawings 1 and embodiment this utility model is further illustrated.
In the embodiment shown in fig. 1, adsorption tower module 2 is made up of two tower process.Deafener module 1 is by flange or quick
Joint is connected with adsorption tower module 2, and adsorption tower module 2 is connected with valve pipeline module 6 and process tank 3 respectively by pipeline, gas
Dynamic model block 5 is connected with valve module 6 and electronic control module 4 by pneumatic line.Each module connect after, connect compressed air and
Instrument supply gas, opens electronic control module 4, and device powers on, and arranges plant running program and time, and instrument supply gas passes through pneumatic line through pneumatic
Module 6 controls valve ducting module 6, and compressed air enters adsorption tower module 2, and device enters duty, according to set
Operation program, left tower absorption in adsorption tower module 2, product gas enters process tank 3, right tower desorbing, tail gas warp in adsorption tower module 2
Discharge of pipes is in deafener module 1, and in adsorption tower module 2 after left tower absorption certain time, in adsorption tower module 2, right tower enters
Adsorbed state, in adsorption tower module 2, left tower carries out desorbing, and so circulation is carried out, output qualified products gas continuously.When wanting
When seeking increase gas production, the quantity of absorption tower system can be increased, when turnover tolerance exceeds the maximal voluntary ventilation of valve pipe, take more
Change larger adsorption tower module, valve pipe module, deafener module and process tank module.
Below in conjunction with the accompanying drawings 2 and embodiment this utility model is further illustrated.
In the embodiment depicted in figure 2, deafener module 1 is connected with membrance separation module 3 by flange or snap joint, and film divides
Being connected with valve pipeline module 2 by pipeline from module 3, Pneumatic module 5 passes through pneumatic line and valve pipe module 2 and automatically controlled
Module 4 is connected.After each module connects, connecting compressed air and instrument supply gas, open electronic control module 4, device powers on, and arranges dress
Putting operation program and time, instrument supply gas controls valve ducting module 2 by pneumatic line through Pneumatic module 5, and compressed air enters
Membrance separation module 3, device enters duty, and tail gas is in discharge of pipes to deafener module 1, and product gas is through valve pipe mould
Block 2 supplies uses gas point, the most continuously output qualified products gas.When requiring to increase gas production, film bucket and phase can be increased
Close the quantity of membrane module, when turnover tolerance exceeds the maximal voluntary ventilation of valve pipe, take to change larger valve pipe mould
Block and deafener module.
Claims (4)
1. a multimode combination type nitrogen production by air separation oxygenerator, it is characterised in that by adsorption tower module or membrance separation module, valve
Door ducting module, deafener module, process tank module, electronic control module and Pneumatic module collectively constitute, and intermodule uses flange, fast
Quick coupling, screw thread or hose connection mode；Adsorption tower module is made up of several adsorption towers and chassis, and adsorption tower module is by two
Tower or multitower composition absorption tower system, but each adsorption tower module is at least made up of two adsorption towers alternately；Membrance separation mould
Block is collectively constituted by one or more film bucket, related film assembly and chassis or support；Valve pipeline module by intake valve, give vent to anger
Valve, air bleeding valve, equalizing valve and admission line, outlet pipe, discharge duct, pressure-equalizing passageway and corresponding manual auxiliary valve and pipe
Road forms；Deafener module is made up of one or more deafeners, and muffler entrance is aggregated in a total air escape pipe road, noise reduction
The additional silencer cover of device module, or be not added with silencer cover, or deafener module entirety is caused equipment storeroom remotely or room
Outward；Electronic control module is made up of Programmable Logic Controller, gas analyser, touch screen, electromagnetic valve and some electric adjuvants, electric adjuvant
For Switching Power Supply, binding post, chopper and insurance, whole automatically controlled part is divided into again four little modules: Programmable Logic Controller mould
Block, gas analyser module, power module, terminal module；Pneumatic module is by some gladhands, flexible pipe, fixed support
Or casing composition, forming including some inlet suction ports and some air outlet adapters, the electromagnetic valve that inlet suction port connects in electronic control module goes out
QI KOU, air outlet adapter connects the pneumatic valve head pilot 3-port transfer in valve pipe module.
A kind of multimode combination type nitrogen production by air separation oxygenerator the most according to claim 1, it is characterised in that described system
Nitrogen oxygenerator, including multimode combination type Nitrogen plant using air separation process and multimode combination type making oxygen by air separation device；Multimode combines
Formula Nitrogen plant using air separation process, including swing adsorption nitrogen producing apparatus and film separation and nitrogen-making device, multimode combination type making oxygen by air separation device,
Including pressure swing adsorption oxygen making device and membrance separation oxygenerator.
A kind of multimode combination type nitrogen production by air separation oxygenerator the most according to claim 1, it is characterised in that valve pipeline
Valve in module is by electromagnetic valve, pneumatically or electrically angle pedestal valve, pneumatically or electrically stop valve, pneumatically or electrically butterfly valve and corresponding
Manual ball valve, needle-valve, gate valve, stop valve, butterfly valve form.
A kind of multimode combination type nitrogen production by air separation oxygenerator the most according to claim 1, it is characterised in that Pneumatic module
For case structure, hipped plate construction or plate armature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620226267.7U CN205803007U (en) | 2016-03-18 | 2016-03-18 | A kind of multimode combination type nitrogen production by air separation oxygenerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620226267.7U CN205803007U (en) | 2016-03-18 | 2016-03-18 | A kind of multimode combination type nitrogen production by air separation oxygenerator |
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| CN205803007U true CN205803007U (en) | 2016-12-14 |
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| Application Number | Title | Priority Date | Filing Date |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112265966A (en) * | 2020-10-22 | 2021-01-26 | 航电中和山东医疗技术有限公司 | Oxygenerator is consolidated to modularization combination formula |
-
2016
- 2016-03-18 CN CN201620226267.7U patent/CN205803007U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112265966A (en) * | 2020-10-22 | 2021-01-26 | 航电中和山东医疗技术有限公司 | Oxygenerator is consolidated to modularization combination formula |
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| DD01 | Delivery of document by public notice |
Addressee: Li Yuxue Document name: Notification of Acceptance of Patent Application |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |