CN107970740A - Zeolite molecular sieve adsorbent equipment - Google Patents
Zeolite molecular sieve adsorbent equipment Download PDFInfo
- Publication number
- CN107970740A CN107970740A CN201610917969.4A CN201610917969A CN107970740A CN 107970740 A CN107970740 A CN 107970740A CN 201610917969 A CN201610917969 A CN 201610917969A CN 107970740 A CN107970740 A CN 107970740A
- Authority
- CN
- China
- Prior art keywords
- device body
- molecular sieve
- zeolite molecular
- sieve adsorbent
- described device
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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Classifications
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/106—Silica or silicates
- B01D2253/108—Zeolites
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
-
- 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
- B01D2259/403—Further details for adsorption processes and devices using three beds
-
- 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
- B01D2259/404—Further details for adsorption processes and devices using four beds
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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)
- Treating Waste Gases (AREA)
Abstract
The present invention relates to a kind of zeolite molecular sieve adsorbent equipment, it includes device body, gas sampling pipeline is equipped with described device body side, opposite side is equipped with discharge tube, gas collection wind turbine is equipped with the gas sampling pipeline, desorption outlet pipe is equipped with the device body of described discharge tube the same side, desorption inlet pipe road is equipped with the device body of described gas sampling pipeline the same side, described device body and gas collection wind turbine are all connected with PLC control devices, and described device body includes at least a zeolite molecular sieve adsorbent bed.High treating effect of the present invention, operating cost is low, securely and reliably.
Description
Technical field
The present invention relates to one kind absorption and regenerating unit, and in particular to a kind of exhaust gas absorption and regenerating unit.
Background technology
Certain exhaust gas can be produced in coating and printing production process, source exhaust gas is that organic solvent volatilization process distributes
's.Existing emission-control equipment, it is small there are adsorbance, because conventional carbon adsorption stripping process accumulation of heat can produce spontaneous combustion, there is safety
Hidden danger, cumbersome, disposed of in its entirety effect is general, and operating cost is high, has secondary pollution generation, and not meeting actual use will
Ask.
The content of the invention
Goal of the invention：The purpose of the invention is to overcome deficiency of the prior art, there is provided a kind of high treating effect, fortune
Row cost is low, safe and reliable zeolite molecular sieve adsorbent equipment.
Technical solution：In order to solve the above-mentioned technical problem, zeolite molecular sieve adsorbent equipment of the present invention, it includes dress
Body is put, is equipped with gas sampling pipeline in described device body side, opposite side is equipped with discharge tube, in the gas sampling pipe
Road is equipped with gas collection wind turbine, desorption outlet pipe is equipped with the device body of described discharge tube the same side, in the exhaust gas
The device body of collection conduit the same side is equipped with desorption inlet pipe road, and described device body and gas collection wind turbine are all controlled with PLC
Device is connected, and described device body includes at least a zeolite molecular sieve adsorbent bed.
The desorption outlet pipe and desorption inlet pipe road are connected with desorption catalyzing regenerating unit respectively.
Described device body is composed in parallel by 3-4 platform zeolite molecular sieve adsorbent beds.
The treating capacity of described device body is 20000m3/h。
Beneficial effect：Compared with prior art, the present invention its remarkable advantage is：It is reasonable that overall structure of the present invention is set, boiling
Stone molecular sieve has the characteristics that non-hypergolic, and large amount of adsorption, is suitable for the VOCs treatment of large-wind-volume low-concentration, using more
Zeolite molecular sieve adsorbent bed composes in parallel device body, large amount of adsorption, and spontaneous combustion will not be produced because of accumulation of heat, safe and reliable,
Zeolite micropore can absorb Organic material, and the organic solvent in large-wind-volume low-concentration Organic exhaust gas is adsorbed onto zeolite molecular sieve
In and concentrate, the gas after adsorption cleaning it is up to standard directly empty, using PLC control devices, system can work automatically, realize
Ease of Use, adaptation concentration range of the invention is big, can daily 24 continuous throughout the twenty-four hour24, high treating effect, operating cost is low, symbol
Close actual operation requirements.
Brief description of the drawings
Fig. 1 is the structure diagram of the present invention.
Embodiment
The present invention is further illustrated with reference to the accompanying drawings and examples.
As shown in Figure 1, zeolite molecular sieve adsorbent equipment of the present invention, it includes device body 1, in described device sheet
1 side of body is equipped with gas sampling pipeline 2, and opposite side is equipped with discharge tube 3, and gas collection wind is equipped with the gas sampling pipeline 2
Machine 4, is equipped with desorption outlet pipe 5 on the device body 1 of described 3 the same side of discharge tube, same in the gas sampling pipeline 2
The device body 1 of side is equipped with desorption inlet pipe road 6, described device body 1 and gas collection wind turbine 4 all with 7 phase of PLC control devices
Even, described device body 1 includes at least a zeolite molecular sieve adsorbent bed 8；The desorption outlet pipe 5 and desorption inlet pipe road
6 are connected with desorption catalyzing regenerating unit 9 respectively；Described device body 1 is composed in parallel by 3-4 platform zeolite molecular sieves adsorbent bed 8；Institute
The treating capacity for stating device body 1 is 20000m3/h.It is reasonable that overall structure of the present invention is set, the non-hypergolic feature of zeolite molecular sieve,
And large amount of adsorption, it is suitable for the VOCs treatment of large-wind-volume low-concentration, is composed in parallel using more zeolite molecular sieve adsorbent beds
Device body, large amount of adsorption, and spontaneous combustion will not be produced because of accumulation of heat, safe and reliable, zeolite micropore can absorb Organic material,
Organic solvent in large-wind-volume low-concentration Organic exhaust gas is adsorbed onto in zeolite molecular sieve and is concentrated, the gas after adsorption cleaning
Body is up to standard directly to be emptied, and using PLC control devices, system can work automatically, realize ease of Use, adaptation concentration of the invention
Scope is big, can daily 24 continuous throughout the twenty-four hour24, high treating effect, operating cost is low, meets actual operation requirements.
The present invention provides a kind of thinking and method, it is many to implement method and the approach of the technical solution, above institute
State only is the preferred embodiment of the present invention, it is noted that for those skilled in the art, is not being departed from
On the premise of the principle of the invention, some improvements and modifications can also be made, these improvements and modifications also should be regarded as the guarantor of the present invention
Scope is protected, all undefined components in this embodiment can be implemented in the prior art.
Claims (4)
1. zeolite molecular sieve adsorbent equipment, it is characterised in that：It includes device body（1）, in described device body（1）Side is set
There is gas sampling pipeline（2）, opposite side is equipped with discharge tube（3）, in the gas sampling pipeline（2）It is equipped with gas collection wind turbine
（4）, in the discharge tube（3）The device body of the same side（1）It is equipped with desorption outlet pipe（5）, in the gas sampling
Pipeline（2）The device body of the same side（1）It is equipped with desorption inlet pipe road（6）, described device body（1）With gas collection wind turbine（4）
All with PLC control devices（7）It is connected, described device body（1）Including at least a zeolite molecular sieve adsorbent bed（8）.
2. zeolite molecular sieve adsorbent equipment according to claim 1, it is characterised in that：The desorption outlet pipe（5）With
Desorption inlet pipe road（6）Respectively with desorption catalyzing regenerating unit（9）It is connected.
3. zeolite molecular sieve adsorbent equipment according to claim 1, it is characterised in that：Described device body（1）By 3-4 platforms
Zeolite molecular sieve adsorbent bed（8）Compose in parallel.
4. zeolite molecular sieve adsorbent equipment according to claim 1, it is characterised in that：Described device body（1）Processing
Measure as 20000m3/h。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610917969.4A CN107970740A (en) | 2016-10-21 | 2016-10-21 | Zeolite molecular sieve adsorbent equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610917969.4A CN107970740A (en) | 2016-10-21 | 2016-10-21 | Zeolite molecular sieve adsorbent equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107970740A true CN107970740A (en) | 2018-05-01 |
Family
ID=62004291
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610917969.4A Pending CN107970740A (en) | 2016-10-21 | 2016-10-21 | Zeolite molecular sieve adsorbent equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107970740A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2579505Y (en) * | 2002-10-31 | 2003-10-15 | 陈泽枝 | Organic waste gas purifying device |
| KR100561253B1 (en) * | 2004-11-03 | 2006-03-15 | 희성엥겔하드주식회사 | Volatile Organic Compound Catalytic Oxidation Treatment System |
| CN2905193Y (en) * | 2006-05-24 | 2007-05-30 | 北京绿创大气环保工程有限责任公司 | An organic waste gas purifier |
| CN105536428A (en) * | 2015-12-14 | 2016-05-04 | 北京蓝博新科环保科技有限公司 | Organic waste gas purification system and purification method |
| CN206121457U (en) * | 2016-10-21 | 2017-04-26 | 无锡云瑞环保设备有限公司 | Zeolite molecular sieve adsorption equipment |
-
2016
- 2016-10-21 CN CN201610917969.4A patent/CN107970740A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2579505Y (en) * | 2002-10-31 | 2003-10-15 | 陈泽枝 | Organic waste gas purifying device |
| KR100561253B1 (en) * | 2004-11-03 | 2006-03-15 | 희성엥겔하드주식회사 | Volatile Organic Compound Catalytic Oxidation Treatment System |
| CN2905193Y (en) * | 2006-05-24 | 2007-05-30 | 北京绿创大气环保工程有限责任公司 | An organic waste gas purifier |
| CN105536428A (en) * | 2015-12-14 | 2016-05-04 | 北京蓝博新科环保科技有限公司 | Organic waste gas purification system and purification method |
| CN206121457U (en) * | 2016-10-21 | 2017-04-26 | 无锡云瑞环保设备有限公司 | Zeolite molecular sieve adsorption equipment |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180501 |