CN106629612A - Equipment capable of separating ozone from oxygen by adsorption and recycling oxygen - Google Patents
Equipment capable of separating ozone from oxygen by adsorption and recycling oxygen Download PDFInfo
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- CN106629612A CN106629612A CN201611045240.9A CN201611045240A CN106629612A CN 106629612 A CN106629612 A CN 106629612A CN 201611045240 A CN201611045240 A CN 201611045240A CN 106629612 A CN106629612 A CN 106629612A
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/10—Preparation of ozone
- C01B13/11—Preparation of ozone by electric discharge
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
- C01B13/0229—Purification or separation processes
- C01B13/0248—Physical processing only
- C01B13/0259—Physical processing only by adsorption on solids
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0001—Separation or purification processing
- C01B2210/0009—Physical processing
- C01B2210/0014—Physical processing by adsorption in solids
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0045—Oxygen
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- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
- Analytical Chemistry (AREA)
Abstract
The invention relates to equipment capable of separating ozone from oxygen by adsorption and recycling oxygen. The equipment is characterized in that an oxygen source, an oxygen buffer tank and an ozone generator are connected sequentially, an outlet of the ozone generator is connected with an adsorption tower I, an adsorption tower II, an adsorption tower III, an adsorption tower IV and an adsorption tower V, first outlets of the five adsorption towers are combined into one way to be connected with an inlet of an oxygen pump, an outlet of the oxygen pump is connected with a second inlet of the oxygen buffer tank, an outlet of an air pump is connected with the five adsorption towers, and second outlets of the five adsorption towers are combined into one way to be connected with an inlet of an ozone storage tank. The equipment has the advantages that low-concentration ozone of one previous adsorption tower can be used for flushing high-concentration ozone in the subsequent adsorption tower, so shat flushing gas consumption is reduced; the equipment is high in oxygen recycling ratio and ozone utilization ratio, low in energy consumption and simple in structure.
Description
Technical field
The present invention relates to ozone preparing technical field, particularly a kind of adsorbable separation ozone is with oxygen and by oxygen recovery
The equipment of recycling.
Background technology
Manufacture ozone have various methods, but mainly two kinds of electrion and DC electrolysis pure water, especially the former, be
The method that the ozone of industry manufacture at present is generally adopted.The advantage of this method is that ozone output is big, technology simple, and prominent asks
The conversion ratio that topic is mainly ozone is too low, and the general conversion ratio in current countries in the world is only 10% or so, that is 100 kilograms
Oxygen is only capable of producing 10 kilograms or so of ozone, and 90 kilograms or so of oxygen is wasted.This causes being manufactured into for ozone
This is high, seriously constrains the application of ozone and the development of ozone industry.Also make with regard to how to improve conversion ratio in the industry
Many effort, but produce little effect, and with the raising of conversion ratio, power consumption also increases, and is not really achieved the mesh of reduces cost
's.Therefore realize the separation of ozone and oxygen and reuse oxygen recovery, be that of reduction ozone manufacturing cost is important
Method.
The content of the invention
It is an object of the invention to overcome the shortcoming of prior art, there is provided a kind of oxygen recovery utilization rate is high, ozone is utilized
Rate height, low energy consumption, simple structure adsorbable separation ozone and oxygen and the equipment for recycling oxygen recovery.
The purpose of the present invention is achieved through the following technical solutions：A kind of adsorbable separation ozone is returned with oxygen and by oxygen
Receive the equipment for recycling, including source of oxygen, oxygen surge tank, ozone generator, adsorption tower I, adsorption tower II, adsorption tower III, suction
Attached tower IV, adsorption tower V, oxygen pump, air pump and ozone storage tank, source of oxygen is connected with the first entrance of oxygen surge tank, oxygen
The outlet of gas surge tank is connected with the entrance of ozone generator, the first entrance for exporting respectively with adsorption tower I of ozone generator,
The first entrance of adsorption tower II, the connection of the first entrance of adsorption tower III, the first entrance connection of adsorption tower IV, the of adsorption tower V
One entrance connects, the first outlet of adsorption tower I, the first outlet of adsorption tower II, the first outlet of adsorption tower III, adsorption tower IV
First outlet, the first outlet of adsorption tower V are combined into and are connected all the way and with the entrance of oxygen pump, and outlet and the oxygen of oxygen pump delay
Rush the second entrance connection of tank, the second entrance for exporting respectively with adsorption tower I of air pump, the second entrance of adsorption tower II, suction
The second entrance connection of attached tower III, the second entrance connection of adsorption tower IV, the second entrance connection of adsorption tower V, adsorption tower I
Second outlet, the second outlet of adsorption tower II, the second outlet of adsorption tower III, the second outlet of adsorption tower IV, adsorption tower V
Second outlet is combined into and is connected all the way and with the entrance of ozone storage tank.
Be provided between the outlet of the ozone generator and the first entrance of adsorption tower V valve A, the of adsorption tower V
Valve B is provided between one outlet and the entrance of oxygen pump, is provided between the outlet of air pump and the second entrance of adsorption tower I
Valve C, is provided with valve D between the second outlet of adsorption tower IV and the entrance of ozone storage tank, the second outlet of adsorption tower I with
Valve E is provided between the second entrance of adsorption tower II, is arranged between the outlet of ozone generator and the first entrance of adsorption tower I
There is valve F, valve G, air pump and the second of adsorption tower II are provided between the first outlet of adsorption tower I and the entrance of oxygen pump
Valve H is provided between entrance, valve I is provided between the second outlet of adsorption tower V and the entrance of ozone storage tank, adsorbed
Valve J, outlet and the adsorption tower II of ozone generator are provided between the second outlet of tower II and the second entrance of adsorption tower III
First entrance between have valve K, have valve L between the first outlet and oxygen pump of adsorption tower II, the outlet of air pump with inhale
There is valve M between the second entrance of attached tower III, have valve N, adsorption tower III between the second outlet and ozone storage tank of adsorption tower I
Second outlet and the second entrance of adsorption tower IV between have a valve O, the 3rd outlet of adsorption tower I enters with the 3rd of adsorption tower II the
Have valve P between mouthful, there is valve Q between the second outlet and ozone storage tank of adsorption tower II, the 3rd outlet of adsorption tower II with
There is valve R between 3rd entrance of adsorption tower III, have valve S, adsorption tower III between the first outlet and oxygen pump of adsorption tower III
First entrance and the outlet of ozone generator between have a valve T, the 3rd outlet of adsorption tower III enters with the 3rd of adsorption tower IV the
There is valve U between mouthful, have valve V, the outlet of air pump and adsorption tower between the second outlet and ozone storage tank of adsorption tower III
There is valve W between IV second entrance, there is valve X between the first entrance of adsorption tower IV and the outlet of ozone generator, adsorb
There is valve Y between the first outlet and oxygen pump of tower IV, between the 3rd outlet of adsorption tower IV and the 3rd entrance of adsorption tower V
There is valve Z, there is valve Z1, outlet and the absorption of air pump between the second outlet of adsorption tower IV and the second entrance of adsorption tower V
There is valve Z2 between the second entrance of tower V, have valve Z3 between the second outlet of adsorption tower V and the second entrance of adsorption tower I,
There is valve Z4 between 3rd outlet of adsorption tower V and the 3rd entrance of adsorption tower I.
Valve A, valve B, valve C, valve D, valve E, valve F, valve G, valve H, valve I, valve J, valve K, valve
Door L, valve M, valve N, valve O, valve P, valve Q, valve R, valve S, valve T, valve U, valve V, valve W, valve X,
Valve Y, valve Z, valve Z1, valve Z2, valve Z3 and valve Z4 are magnetic valve or pneumatic operated valve.
The present invention has advantages below：
1st, using ozone adsorption technology, by obtained ozone and oxygen separation, enabling the ozone recovery of more than 80% waste makes
With greatly reducing the manufacturing cost of ozone.
2nd, device structure is simple, it is easy to operate, and equipment operation automation, energy consumption is low.
Description of the drawings
Fig. 1 is the structural representation of the present invention；
In figure：1- source of oxygen, 2- oxygen surge tanks, 3- ozone generators, 4- adsorption towers I, 5- adsorption towers II, 6- adsorption towers III,
7- adsorption towers IV, 8- adsorption towers V, 9- ozone storage tanks, 10- air pumps, 11- oxygen pumps, 12- valve A, 13- valve B,
14- valve C, 15 valve D, 16- valve E, 17- valve F, 18- valve G, 19- valve H, 20- valve I, 21- valve J, 22- valves
Door K, 23- valve L, 24- valve M, 25- valve N, 26- valve O, 27- valve P, 28- valve Q, 29- valve R, 30- valve S,
31- valve T, 32- valve U, 33- valve V, 34- valve W, 35- valve X, 36- valve Y, 37- valve Z, 38- valve Z1,39-
Valve Z2,40- valve Z3,41- valve Z4.
Specific embodiment
Below in conjunction with the accompanying drawings the present invention will be further described, but protection scope of the present invention is not limited to following institute
State.
As shown in figure 1, a kind of adsorbable equipment for separating ozone and oxygen and recycling oxygen recovery, including source of oxygen
1st, oxygen surge tank 2, ozone generator 3, adsorption tower I 4, adsorption tower II 5, adsorption tower III 6, adsorption tower IV 7, adsorption tower V 8, smelly
Oxygen holding vessel 9, air pump 10 and oxygen pump 11, adsorption tower I 4, adsorption tower II 5, adsorption tower III 6, adsorption tower IV 7, adsorption tower V 8
The ozone adsorbent inside placed respectively is material disclosed in Chinese patent 201410038140.8, source of oxygen 1 and oxygen surge tank 2
First entrance connection, the outlet of oxygen surge tank 2 is connected with the entrance of ozone generator 3, and the outlet of ozone generator 3 is distinguished
First entrance, the first entrance of adsorption tower II 5 with adsorption tower I 4, the first entrance of adsorption tower III 6 be connected, adsorption tower IV 7
First entrance connection, the first entrance connection of adsorption tower V 8, the first outlet of adsorption tower I 4, the first outlet of adsorption tower II 5,
The first outlet of adsorption tower III 6, the first outlet of adsorption tower IV 7, the first outlet of adsorption tower V 8 be combined into all the way and with oxygen pump
11 entrance connection, the outlet of oxygen pump 11 is connected with the second entrance of oxygen surge tank 2, the outlet of air pump 10 respectively with suction
The second entrance of attached tower I 4, the second entrance of adsorption tower II 5, the second entrance of adsorption tower III 6, the second entrance of adsorption tower IV 7,
The second entrance connection of adsorption tower V 8, the second outlet of adsorption tower I 4, the second outlet of adsorption tower II 5, the of adsorption tower III 6
Two outlets, the second outlet of adsorption tower IV 7, the second outlet of adsorption tower V 8 are combined into and connect all the way and with the entrance of ozone storage tank 9
Connect.
Valve A12, adsorption tower V 8 are provided between the outlet of the ozone generator 3 and the first entrance of adsorption tower V 8
First outlet and the entrance of oxygen pump 11 between be provided with valve B13, the outlet of air pump 10 enters with the second of adsorption tower I 4
Valve C14 is provided between mouthful, between the second outlet of adsorption tower IV 7 and the entrance of ozone storage tank 9 valve D15 is provided with,
Be provided with valve E16 between the second outlet of adsorption tower I 4 and the second entrance of adsorption tower II 5, the outlet of ozone generator 3 with
Valve F17 is provided between the first entrance of adsorption tower I 4, is set between the first outlet of adsorption tower I 4 and the entrance of oxygen pump 11
It is equipped between the second entrance of valve G18, air pump 10 and adsorption tower II 5 and is provided with valve H19, the second of adsorption tower V 8 goes out
Valve I20 is provided between mouth and the entrance of ozone storage tank 9, the second outlet of adsorption tower II 5 enters with the second of adsorption tower III 6
Valve J21 is provided between mouthful, there is valve K22 between the outlet of ozone generator 3 and the first entrance of adsorption tower II 5, adsorbed
Have valve L23 between the first outlet and oxygen pump 11 of tower II 5, the outlet of air pump 10 and the second entrance of adsorption tower III 6 it
Between have valve M24, have valve N25, the second outlet of adsorption tower III 6 between the second outlet and ozone storage tank 9 of adsorption tower I 4
Have valve O26 and the second entrance of adsorption tower IV 7 between, the 3rd outlet of adsorption tower I 4 and the 3rd entrance of adsorption tower II 5 it
Between have valve P27, have valve Q28, adsorption tower II 5 between the second outlet and ozone storage tank 9 of adsorption tower II 5 the 3rd goes out
There is valve R29 between mouth and the 3rd entrance of adsorption tower III 6, have valve between the first outlet and oxygen pump 11 of adsorption tower III 6
S30, there is valve T31, the 3rd outlet of adsorption tower III 6 between the first entrance of adsorption tower III 6 and the outlet of ozone generator 3
There is valve U32 and the 3rd entrance of adsorption tower IV 7 between, have valve between the second outlet and ozone storage tank 9 of adsorption tower III 6
V33, there is a valve W34 between the outlet of air pump 10 and the second entrance of adsorption tower IV 7, the first entrance of adsorption tower IV 7 with it is smelly
There is valve X35 between the outlet of Oxygen Generator 3, have valve Y36 between the first outlet and oxygen pump 11 of adsorption tower IV 7, adsorb
There are valve Z37, the second outlet and adsorption tower of adsorption tower IV 7 between 3rd outlet of tower IV 7 and the 3rd entrance of adsorption tower V 8
There is valve Z138 between V 8 second entrance, have valve between the outlet of air pump 10 and the second entrance of adsorption tower V 8
Z239, have valve Z340, adsorption tower V 8 between the second outlet of adsorption tower V 8 and the second entrance of adsorption tower I 4 the 3rd goes out
There is valve Z441 between mouth and the 3rd entrance of adsorption tower I 4.
Valve A12, valve B13, valve C14, valve D15, valve E16, valve F17, valve G18, valve H19, valve
I20, valve J21, valve K22, valve L23, valve M24, valve N25, valve O26, valve P27, valve Q28, valve R29,
Valve S30, valve T31, valve U32, valve V33, valve W34, valve X35, valve Y36, valve Z37, valve Z138, valve
Z239, valve Z340 and valve Z441 are magnetic valve or pneumatic operated valve.
The course of work of the present invention is as follows：Source of oxygen 1 is input into oxygen in oxygen surge tank 2, after pressure stability, by oxygen
Ozone generator 3 is delivered to, the mixed gas of ozone and oxygen, Open valve A12, valve Z441 and valve are produced by corona discharge
The mixed gas of door G18, ozone and oxygen enter adsorption tower V 8 and adsorption tower I 4 through valve A12, and ozone and oxygen are carried out
Adsorbing separation, ozone is adsorbed, and the oxygen isolated enters oxygen surge tank 2, tower to be adsorbed by valve G18 and oxygen pump 11
V 8 with the adsorption saturation of adsorption tower I 4 after, close valve A12, valve G18 and valve Z441, open valve F17, valve L23, valve
Door P27, valve I20, valve Z138, valve O26 and valve M24, allow ozone and oxygen mixed gas enter adsorption tower I 4 with
In adsorption tower II 5, ozone and oxygen are separated, ozone is adsorbed, the oxygen isolated enters oxygen by valve L23 and oxygen pump 11
Gas surge tank 2, while air is pressurizeed by air pump 10, is rinsed in adsorption tower V 8 by valve Z138, valve O26 and valve M24
Ozone, then by valve I20 enter ozone surge tank 9；After adsorption tower I 4 and II 5 adsorption saturation of adsorption tower, valve is closed
F17, valve L23, valve P27, valve M24, valve O26, valve I20, Open valve K22, valve R29, valve S30, valve
W34, valve Z340 and valve N25, allow the mixed gas of ozone and oxygen to enter in adsorption tower II 5 and adsorption tower III 6, separate smelly
Oxygen and oxygen, ozone is adsorbed, and the oxygen isolated enters oxygen surge tank 2 by valve S30 and oxygen pump 11, while air
Pressurizeed by air pump 10, the ozone rinsed in adsorption tower I 4 by valve W34, valve Z138 and valve Z340, then by valve
N25 enters ozone surge tank 9；After adsorption tower II 5 and III 6 adsorption saturation of adsorption tower, valve K22, valve R29, valve are closed
S30, valve W34, valve Z138 and valve N25, Open valve T31, valve U32, valve Y36, valve Z239, valve E16 and
Valve Q28, allow ozone and oxygen mixed gas enter adsorption tower III 6 and adsorption tower IV 7 with it is interior, separate ozone and oxygen, general
Ozone adsorbs, and the oxygen isolated enters oxygen surge tank 2 by valve Y36 and oxygen pump 11, while air is by air pump 10
Pressurization, the ozone rinsed in adsorption tower II 5 by valve Z239, valve Z340, valve E16, then ozone is entered by valve Q28
Surge tank 9.After adsorption tower III 6 and IV 7 adsorption saturation of adsorption tower, valve T31, valve U32, valve Y36, valve are closed
Z239, valve Z340 and valve Q28, Open valve X35, valve Z37, valve B13, valve J21, valve C14 and valve V33,
Allow the mixed gas of ozone and oxygen to enter in adsorption tower IV 7 and adsorption tower V 8, separate ozone and oxygen, ozone is adsorbed, point
The oxygen for separating out enters oxygen surge tank 2 by valve B13 and oxygen pump 11, while air is pressurizeed by air pump 10, by valve
The ozone that door C14, valve E16, valve J21 are rinsed in adsorption tower III 6, then ozone surge tank 9 is entered by valve V33.Work as suction
After attached tower IV 7 and the adsorption saturation of adsorption tower V 8, valve X35, valve Z37, valve B13, valve C14, valve E16 and valve are closed
Door V33, opens Z441, valve G18, valve A12, valve H19, valve O26 and valve D15, allows the gaseous mixture of ozone and oxygen
Body is entered in adsorption tower V 8 and adsorption tower I 4, separates ozone and oxygen, and ozone is adsorbed, and the oxygen isolated passes through valve G18
Oxygen surge tank 2 is entered with oxygen pump 11, while air is pressurizeed by air pump 10, by valve H19, valve J21, valve O26
The ozone rinsed in adsorption tower IV 7, then ozone surge tank 9 is entered by valve D15.
Repeat flow process above, adsorption tower I 4, adsorption tower II 5, adsorption tower III 6, adsorption tower IV 7, adsorption tower V 8 work successively
Being continuously separated for ozone and oxygen is formed, whole flow process is automatically performed by PLC controls.
Embodiments of the invention disclose only the form of five towers absorption, it shall be apparent to one skilled in the art that its
Still the technical scheme described in foregoing embodiments can be modified, such as the even more many absorption of three towers, four towers, six towers
The similar attachment structure of tower, or equivalent is carried out to which part technical characteristic, it is all the spirit and principles in the present invention it
Interior, any modification, equivalent substitution and improvements made etc. should be included within the scope of the present invention.
Claims (3)
1. the equipment that a kind of adsorbable separation ozone is recycled with oxygen and by oxygen recovery, it is characterised in that：Including source of oxygen
（1）, oxygen surge tank（2）, ozone generator（3）, adsorption tower I（4）, adsorption tower II（5）, adsorption tower III（6）, adsorption tower IV
（7）, adsorption tower V（8）, ozone storage tank（9）, air pump（10）With oxygen pump（11）, source of oxygen（1）With oxygen surge tank（2）
First entrance connection, oxygen surge tank（2）Outlet and ozone generator（3）Entrance connection, ozone generator（3）Go out
Mouth respectively with adsorption tower I（4）First entrance, adsorption tower II（5）First entrance, adsorption tower III（6）First entrance, absorption
Tower IV（7）First entrance, adsorption tower V（8）First entrance connection, adsorption tower I（4）First outlet, adsorption tower II（5）
First outlet, adsorption tower III（6）First outlet, adsorption tower IV（7）First outlet, adsorption tower V（8）First outlet
Be combined into all the way and with oxygen pump（11）Entrance connection, oxygen pump（11）Outlet and oxygen surge tank（2）Second entrance connect
Connect, air pump（10）Outlet respectively with adsorption tower I（4）Second entrance, adsorption tower II（5）Second entrance, adsorption tower III
（6）Second entrance, adsorption tower IV（7）Second entrance, adsorption tower V（8）Second entrance connection, adsorption tower I（4）
Two outlets, adsorption tower II（5）Second outlet, adsorption tower III（6）Second outlet, adsorption tower IV（7）Second outlet, absorption
Tower V（8）Second outlet be combined into all the way and with ozone storage tank（9）Entrance connection.
2. the equipment that a kind of adsorbable separation ozone according to claim 1 is recycled with oxygen and by oxygen recovery, its
It is characterised by：The ozone generator（3）Outlet and adsorption tower V（8）First entrance between be provided with valve A（12）, inhale
Attached tower V（8）First outlet and oxygen pump（11）Entrance between be provided with valve B（13）, air pump（10）Outlet with inhale
Attached tower I（4）Second entrance between be provided with valve C（14）, adsorption tower IV（7）Second outlet and ozone storage tank（9）'s
Valve D is provided between entrance（15）, adsorption tower I（4）Second outlet and adsorption tower II（5）Second entrance between be provided with
Valve E（16）, ozone generator（3）Outlet and adsorption tower I（4）First entrance between be provided with valve F（17）, adsorption tower
Ⅰ（4）First outlet and oxygen pump（11）Entrance between be provided with valve G（18）,
Air pump（10）With adsorption tower II（5）Second entrance between be provided with valve H（19）, adsorption tower V（8）Second go out
Mouth and ozone storage tank（9）Entrance between be provided with valve I（20）, adsorption tower II（5）Second outlet and adsorption tower III（6）
Second entrance between be provided with valve J（21）, ozone generator（3）Outlet and adsorption tower II（5）First entrance between
There is valve K（22）, adsorption tower II（5）First outlet and oxygen pump（11）Between have valve L（23）, air pump（10）Outlet
With adsorption tower III（6）Second entrance between have valve M（24）, adsorption tower I（4）Second outlet and ozone storage tank（9）It
Between have valve N（25）, adsorption tower III（6）Second outlet and adsorption tower IV（7）Second entrance between have valve O（26）, inhale
Attached tower I（4）The 3rd outlet with adsorption tower II（5）The 3rd entrance between have valve P（27）, adsorption tower II（5）Second go out
Mouth and ozone storage tank（9）Between have valve Q（28）, adsorption tower II（5）The 3rd outlet with adsorption tower III（6）The 3rd enter
There is valve R between mouthful（29）, adsorption tower III（6）First outlet and oxygen pump（11）Between have valve S（30）, adsorption tower III
（6）First entrance and ozone generator（3）Outlet between have valve T（31）, adsorption tower III（6）The 3rd outlet with inhale
Attached tower IV（7）The 3rd entrance between have valve U（32）, adsorption tower III（6）Second outlet and ozone storage tank（9）Between have
Valve V（33）, air pump（10）Outlet and adsorption tower IV（7）Second entrance between have valve W（34）, adsorption tower IV（7）
First entrance and ozone generator（3）Outlet between have valve X（35）, adsorption tower IV（7）First outlet and oxygen pump
（11）Between have valve Y（36）, adsorption tower IV（7）The 3rd outlet with adsorption tower V（8）The 3rd entrance between have valve Z
（37）, adsorption tower IV（7）Second outlet and adsorption tower V（8）Second entrance between have valve Z1（38）, air pump（10）
Outlet and adsorption tower V（8）Second entrance between have valve Z2（39）, adsorption tower V（8）Second outlet and adsorption tower I
（4）Second entrance between have valve Z3（40）, adsorption tower V（8）The 3rd outlet with adsorption tower I（4）The 3rd entrance between
There is valve Z4（41）.
3. the equipment that a kind of adsorbable separation ozone according to claim 2 is recycled with oxygen and by oxygen recovery, its
It is characterised by：Valve A（12）, valve B（13）, valve C（14）, valve D（15）, valve E（16）, valve F（17）, valve G
（18）, valve H（19）, valve I（20）, valve J（21）, valve K（22）, valve L（23）, valve M（24）, valve N（25）, valve
Door O（26）, valve P（27）, valve Q（28）, valve R（29）, valve S（30）, valve T（31）, valve U（32）, valve V
（33）, valve W（34）, valve X（35）, valve Y（36）, valve Z（37）, valve Z1（38）, valve Z2（39）, valve Z3（40）
With valve Z4（41）For magnetic valve or pneumatic operated valve.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2016104319053 | 2016-06-17 | ||
| CN201610431905.3A CN105836713A (en) | 2016-06-17 | 2016-06-17 | Device for separating ozone and oxygen by adsorption and recycling oxygen |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106629612A true CN106629612A (en) | 2017-05-10 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610431905.3A Pending CN105836713A (en) | 2016-06-17 | 2016-06-17 | Device for separating ozone and oxygen by adsorption and recycling oxygen |
| CN201611045240.9A Pending CN106629612A (en) | 2016-06-17 | 2016-11-24 | Equipment capable of separating ozone from oxygen by adsorption and recycling oxygen |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610431905.3A Pending CN105836713A (en) | 2016-06-17 | 2016-06-17 | Device for separating ozone and oxygen by adsorption and recycling oxygen |
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| CN (2) | CN105836713A (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN112604476A (en) * | 2020-12-29 | 2021-04-06 | 浙江百能科技有限公司 | Method for recycling oxygen in boiler flue gas ozone oxidation denitration process |
| CN113501503B (en) * | 2021-07-01 | 2024-04-02 | 光大水务科技发展（南京）有限公司 | Ozone separation system and method for generating high-concentration ozone based on desorption ozone reblowing |
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|---|---|---|---|---|
| CN2250348Y (en) * | 1996-03-13 | 1997-03-26 | 中国科学院物理研究所 | Novel high-purity ozone device of structure |
| CN101878183A (en) * | 2007-11-30 | 2010-11-03 | 东芝三菱电机产业系统株式会社 | High-concentrated ozone gas generating device and high-concentrated ozone gas generation method |
| CN201722145U (en) * | 2010-06-30 | 2011-01-26 | 深圳市深港产学研环保工程技术股份有限公司 | Ozone generation system and sewage treatment system |
| CN202880876U (en) * | 2012-11-12 | 2013-04-17 | 蹇守民 | Equipment for preparing high-concentration ozone and recycling and reusing residual oxygen |
| CN103754829A (en) * | 2014-01-27 | 2014-04-30 | 蹇守民 | Method for separating oxygen from ozone |
-
2016
- 2016-06-17 CN CN201610431905.3A patent/CN105836713A/en active Pending
- 2016-11-24 CN CN201611045240.9A patent/CN106629612A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2250348Y (en) * | 1996-03-13 | 1997-03-26 | 中国科学院物理研究所 | Novel high-purity ozone device of structure |
| CN101878183A (en) * | 2007-11-30 | 2010-11-03 | 东芝三菱电机产业系统株式会社 | High-concentrated ozone gas generating device and high-concentrated ozone gas generation method |
| CN201722145U (en) * | 2010-06-30 | 2011-01-26 | 深圳市深港产学研环保工程技术股份有限公司 | Ozone generation system and sewage treatment system |
| CN202880876U (en) * | 2012-11-12 | 2013-04-17 | 蹇守民 | Equipment for preparing high-concentration ozone and recycling and reusing residual oxygen |
| CN103754829A (en) * | 2014-01-27 | 2014-04-30 | 蹇守民 | Method for separating oxygen from ozone |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105836713A (en) | 2016-08-10 |
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Application publication date: 20170510 |