CN208372763U - A kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipment - Google Patents
A kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipment Download PDFInfo
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- CN208372763U CN208372763U CN201820611355.8U CN201820611355U CN208372763U CN 208372763 U CN208372763 U CN 208372763U CN 201820611355 U CN201820611355 U CN 201820611355U CN 208372763 U CN208372763 U CN 208372763U
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- oil cotton
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Abstract
The utility model discloses a kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipments, including adsorption tanks ontology, adsorption tanks ontology is internally provided with adsorption element, adsorption element includes matrix, matrix is annular, matrix is provided centrally with ogive, ogive is protruded to simulation model for mixing gases flows direction to be arranged, fluorosilicon oil cotton is attached on matrix, ogive, silicone oil cotton is attached to the outer surface of adsorption element, the ogive of protrusion setting increases the contact area of fluorosilicon oil cotton and mixed gas, and the Vapor adsorption effect of fluorosilicon oil cotton adsorbent equipment is preferable；The front end of adsorption tanks ontology is provided with air inlet simultaneously, air inlet is connected with the equal cloth component of dispersion, the fluorosilicon oil cotton adsorbent equipment mixed gas is uniformly dispersed when entering, so that the mixed gas into fluorosilicon oil cotton is more uniform, so that the Vapor adsorption effect of fluorosilicon oil cotton adsorbent equipment is preferable.
Description
Technical field
The utility model relates to a kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipments, specifically, being related to one kind
The preferable fluorosilicon oil cotton adsorbent equipment of adsorption effect, belongs to useless low mercury catalyst recovery technology field.
Background technique
Useless low mercury catalyst recycling recovery process the following steps are included:
(1) useless mercuric chloride catalyst is placed in gas retort, is passed through nitrogen from the bottom of gas retort, displaces in gas retort
Air, then by the pressure control in gas retort in -0.09-0MPa, by gas retort heat temperature raising, temperature is 500-600 DEG C, is obtained
To the mixed gas of recovered carbon and chloride containing mercury, nitrogen；
(2) mixed gas enters cooler, and cooling obtains mercury chloride powder；Mixed gas enters cooler cooling and also obtains
Residual exhaust；
(3) residual exhaust enters water washing tank and is washed, and enters back into caustic treater and is neutralized；It is inhaled subsequently into fluorosilicon oil cotton
Attached tank removes water mist, then enters primary activity charcoal adsorption tanks through fluorosilicon oil cotton adsorption tanks and adsorbed, then in the effect of vacuum pump
It is lower to be adsorbed into second order activity charcoal adsorption tanks, obtain circulating nitrogen gas.
Recyclable device includes the gas retort of connection, cooler, water washing tank, caustic treater, fluorosilicon oil cotton adsorption tanks, primary activity
Charcoal adsorption tanks, second order activity charcoal adsorption tanks and vacuum pump.
Useless low mercury catalyst recycling is inhaled with the recovery process absorption for being carried out water mist using fluorosilicon oil cotton adsorption tanks, fluorosilicon oil cotton
Attached tank includes adsorption tanks ontology, and adsorption tanks ontology has air inlet pipe and an air outlet pipe, and the level that is internally provided with of adsorption tanks ontology is set
It is equipped with the fixed net of several bilayers, is provided with fluorosilicon oil cotton in the interlayer of the fixed net of bilayer, fluorosilicon oil cotton is for adsorbing gaseous mixture
Water mist in body, currently, fluorosilicon oil cotton adsorption tanks enter the mixed gas of nitrogen and water mist from air inlet pipe, nitrogen and water mist it is mixed
Closing dispersion when gas enters, unevenly, the adsorption effect for causing fluorosilicon oil cotton to adsorb is poor, meanwhile, it is horizontally set on fluorosilicon oil cotton
Adsorption area is smaller, and the adsorption effect that will also result in the absorption of fluorosilicon oil cotton is poor.
Utility model content
The technical problems to be solved in the utility model is against the above deficiency, to provide a kind of useless low mercury catalyst recycling fluorine silicon
Oily cotton adsorbent equipment, the fluorosilicon oil cotton adsorbent equipment fluorosilicon oil cotton adsorption area is larger, and the steam of fluorosilicon oil cotton adsorbent equipment is inhaled
Attached effect is preferable；
It is uniformly dispersed when the fluorosilicon oil cotton adsorbent equipment mixed gas enters simultaneously, so that into the gaseous mixture of fluorosilicon oil cotton
Body is more uniform, so that the Vapor adsorption effect of fluorosilicon oil cotton adsorbent equipment is preferable.
In order to solve the above technical problems, the utility model uses following technical scheme: fluorine is used in a kind of useless low mercury catalyst recycling
Silicone oil cotton adsorbent equipment, including adsorption tanks ontology, it is characterised in that: the adsorption tanks ontology is internally provided with adsorption element,
Adsorption element is fixed on supporting member, and adsorption element is several, several adsorption elements are perpendicular to mixed gas stream
Dynamic direction setting；
The adsorption element includes matrix, and matrix is annular, and matrix is provided centrally with ogive, and ogive is to gaseous mixture
The protrusion setting of body flow direction, matrix, ogive are ventilative reticular structure, and fluorosilicon oil cotton is attached on matrix, ogive,
Silicone oil cotton is attached to the outer surface of adsorption element；
The supporting member is annular, and supporting member has an inner wall and an outer wall, sets on the inside of supporting member
It is equipped with card slot, the base mate use of card slot and adsorption element.
A kind of scheme of optimization, the front end of the adsorption tanks ontology are provided with air inlet, and it is uniformly distributed that air inlet is connected with dispersion
Component；
The equal cloth component of dispersion includes the first uniformly distributed room, and the first uniformly distributed room is connected with air inlet.
Described first uniformly distributed room is connected with the second uniformly distributed room, and the first uniformly distributed room is provided with and communicated with first with the second uniformly distributed room
Cloth hole；
Described first uniformly distributed room, the second outside for being evenly distributed with room are provided with third and are evenly distributed with room, and the second uniformly distributed room and third are uniformly distributed
Room is provided with and communicated with the second equal cloth hole, and third, which is evenly distributed on room, is provided with the equal cloth hole of third.
Further, the supporting member is fixedly connected with adsorption tanks ontology, and supporting member and adsorption element are clamped, absorption
Fluorosilicon oil cotton is attached on component, fluorosilicon oil cotton is used to adsorb the water mist in mixed gas.
Further, the third is evenly distributed with the outer wall of room and adsorption tanks ontology fits.
Further, the rear end of the adsorption tanks ontology is provided with gas outlet, and the lower part of adsorption tanks ontology is provided with support
Seat.
The utility model after the above technical solution is adopted, compared with prior art, has the advantage that one kind is given up the touching of low mercury
Matchmaker recycles with fluorosilicon oil cotton adsorbent equipment, including adsorption tanks ontology, and adsorption tanks ontology is internally provided with adsorption element, adsorbs structure
Part includes matrix, and matrix is annular, and matrix is provided centrally with ogive, and ogive is set to simulation model for mixing gases flows direction protrusion
It sets, fluorosilicon oil cotton is attached on matrix, ogive, silicone oil cotton is attached to the outer surface of adsorption element, protrudes the ogive of setting
The contact area of fluorosilicon oil cotton and mixed gas is increased, the Vapor adsorption effect of fluorosilicon oil cotton adsorbent equipment is preferable；
The front end of adsorption tanks ontology is provided with air inlet simultaneously, and air inlet is connected with the equal cloth component of dispersion, the fluorosilicon oil cotton
Adsorbent equipment mixed gas is uniformly dispersed when entering, so that the mixed gas into fluorosilicon oil cotton is more uniform, so that fluorine
The Vapor adsorption effect of silicone oil cotton adsorbent equipment is preferable.
The utility model is described in detail with reference to the accompanying drawings and examples.
Detailed description of the invention
Attached drawing 1 is the structural schematic diagram of fluorosilicon oil cotton adsorbent equipment in the utility model embodiment；
Attached drawing 2 is the structural schematic diagram of adsorption element in the utility model embodiment；
Attached drawing 3 is the structural schematic diagram of supporting member in the utility model embodiment；
Attached drawing 4 is the structural schematic diagram for dispersing equal cloth component in the utility model embodiment；
In figure,
1- adsorption tanks ontology, 2- adsorption element, 3- supporting member, 4- matrix, 5- ogive, 6- card slot, 7- air inlet, 8-
Disperse equal cloth component, 9- first is evenly distributed with room, and 10- second is evenly distributed with room, the equal cloth hole of 11- first, and 12- third is evenly distributed with room, and 13- second is equal
Cloth hole, the equal cloth hole of 14- third, the gas outlet 15-, 16- support base.
Specific embodiment
For a clearer understanding of the technical features, objectives and effects of the utility model, now compareing Detailed description of the invention
Specific embodiment of the present utility model.
Embodiment, as shown in Figure 1, Figure 2, Figure 3, Figure 4, a kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipment, packet
Adsorption tanks ontology 1 is included, adsorption tanks ontology 1 is internally provided with adsorption element 2, and adsorption element 2 is fixed at supporting member 3
On, adsorption element 2 is several, several adsorption elements 2 are arranged perpendicular to simulation model for mixing gases flows direction.
Adsorption element 2 includes matrix 4, and matrix 4 is annular, and matrix 4 is provided centrally with ogive 5, and ogive 5 is to mixing
Gas flow direction protrusion setting, matrix 4, ogive 5 are ventilative reticular structure, are attached with fluorine on matrix 4, ogive 5
Silicone oil cotton, silicone oil cotton are attached to the outer surface of adsorption element 2, and the ogive 5 for protruding setting increases fluorosilicon oil cotton and gaseous mixture
The Vapor adsorption effect of the contact area of body, fluorosilicon oil cotton adsorbent equipment is preferable；Supporting member 3 is annular, and supporting member 3 has
One inner wall and an outer wall, card slot 6 is provided on the inside of supporting member 3, and the cooperation of matrix 4 of card slot 6 and adsorption element 2 makes
With.
Supporting member 3 is fixedly connected with attached tank ontology 1, and supporting member 3 and adsorption element 2 are clamped, and is adhered on adsorption element 2
There is fluorosilicon oil cotton, fluorosilicon oil cotton is used to adsorb the water mist in mixed gas.
The front end of adsorption tanks ontology 1 is provided with air inlet 7, and air inlet 7 is connected with the equal cloth component 8 of dispersion, disperses uniformly distributed structure
Part 8 includes the first uniformly distributed room 9, and the first uniformly distributed room 9 is connected with air inlet 7.
First uniformly distributed room 9 is connected with the second uniformly distributed room 10, and the first uniformly distributed room 9 and the second uniformly distributed room 10 are provided with and communicated with first
Equal cloth hole 11.
The outside that first uniformly distributed room 9, second is evenly distributed with room 10 is provided with third and is evenly distributed with room 12, and the second uniformly distributed room 10 and third are equal
Cloth room 12 is provided with and communicated with the second equal cloth hole 13, and third, which is evenly distributed on room 12, is provided with the equal cloth hole 14 of third.
Third is evenly distributed with the outer wall of room 12 and adsorption tanks ontology 1 fits.
Mixed gas enters the first uniformly distributed room 9 from air inlet 7, carries out first time mixing in the first uniformly distributed room 9, then from the
One equal cloth hole 11 enters the second uniformly distributed room 10, carries out second in the second uniformly distributed room 10 and mixes, then from the second equal cloth hole 13 into
Enter third and be evenly distributed with room 12, be evenly distributed in room 12 progress third time mixing in third, then from equal 14 flow forward of cloth hole of third, the fluorine silicon
Oily cotton adsorbent equipment mixed gas is uniformly dispersed when entering, so that the mixed gas into fluorosilicon oil cotton is more uniform, makes
The Vapor adsorption effect for obtaining fluorosilicon oil cotton adsorbent equipment is preferable.
The rear end of adsorption tanks ontology 1 is provided with gas outlet 15, and the lower part of adsorption tanks ontology 1 is provided with support base 16.
Note: the arrow in Figure of description indicates the flow direction of mixed gas.
The same or similar label correspond to the same or similar components in the attached drawing of the utility model embodiment；It is practical at this
In novel description, it is to be understood that if there is the finger such as term " on ", "lower", "left", "right", "top", "bottom", "inner", "outside"
The orientation or positional relationship shown be based on the orientation or positional relationship shown in the drawings, be merely for convenience of description the utility model and
Simplify description, rather than the device or element of indication or suggestion meaning must have a particular orientation, with specific orientation construction
And operation, therefore the terms describing the positional relationship in the drawings are only for illustration, should not be understood as the limitation to this patent.
In addition, if there is the terms such as " first ", " second " to be used for description purposes only, be mainly used for distinguishing different devices,
Element or component (specific type and construction may identical may also be different), is not intended to show or implies indicated fill
It sets, the relative importance and quantity of element or component, and should not be understood as indicating or implying relative importance.
The above specific embodiments are only exemplary, is to enable those skilled in the art to better understand this
Utility model content should not be understood as the limitation to scope of protection of the utility model, as long as according to the utility model technology
Scheme improvements introduced, each falls within the protection scope of the utility model.
Claims (5)
1. a kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipment, including adsorption tanks ontology (1), it is characterised in that: described
Adsorption tanks ontology (1) is internally provided with adsorption element (2), and adsorption element (2) is fixed on supporting member (3), absorption
Component (2) is several, several adsorption elements (2) are arranged perpendicular to simulation model for mixing gases flows direction；
The adsorption element (2) includes matrix (4), and matrix (4) is annular, and matrix (4) is provided centrally with ogive (5), is encircleed
Body (5) is protruded to simulation model for mixing gases flows direction to be arranged, and matrix (4), ogive (5) are ventilative reticular structure, matrix
(4), it is attached with fluorosilicon oil cotton on ogive (5), silicone oil cotton is attached to the outer surface of adsorption element (2)；
The supporting member (3) is annular, and supporting member (3) has an inner wall and an outer wall, the inside of supporting member (3)
On be provided with card slot (6), card slot (6) and the matrix (4) of adsorption element (2) are used cooperatively.
2. a kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipment as described in claim 1, it is characterised in that: the suction
The front end of attached tank ontology (1) is provided with air inlet (7), and air inlet (7) is connected with the equal cloth component (8) of dispersion；
The equal cloth component (8) of dispersion includes first uniformly distributed room (9), and first uniformly distributed room (9) are connected with air inlet (7)；
Described first uniformly distributed room (9) are connected with second uniformly distributed room (10), and first uniformly distributed room (9) are connected to second uniformly distributed room (10) and set
It is equipped with the first equal cloth hole (11)；
Described first uniformly distributed room (9), the second outside for being evenly distributed with room (10) are provided with third and are evenly distributed with room (12), second uniformly distributed room (10)
Room (12) is evenly distributed with third and is provided with and communicated with the second equal cloth hole (13), and third, which is evenly distributed on room (12), is provided with the equal cloth hole of third
(14).
3. a kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipment as described in claim 1, it is characterised in that: the branch
Support component (3) is fixedly connected with adsorption tanks ontology (1), and supporting member (3) and adsorption element (2) are clamped, attached on adsorption element (2)
Have a fluorosilicon oil cotton, fluorosilicon oil cotton is used to adsorb the water mist in mixed gas.
4. a kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipment as claimed in claim 2, it is characterised in that: described the
The outer wall of three uniformly distributed room (12) fits with adsorption tanks ontology (1).
5. a kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipment as described in claim 1, it is characterised in that: the suction
The rear end of attached tank ontology (1) is provided with gas outlet (15), and the lower part of adsorption tanks ontology (1) is provided with support base (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820611355.8U CN208372763U (en) | 2018-04-26 | 2018-04-26 | A kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820611355.8U CN208372763U (en) | 2018-04-26 | 2018-04-26 | A kind of useless low mercury catalyst recycling fluorosilicon oil cotton adsorbent equipment |
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| Publication Number | Publication Date |
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| CN208372763U true CN208372763U (en) | 2019-01-15 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112387050A (en) * | 2020-11-13 | 2021-02-23 | 攀枝花钢企欣宇化工有限公司 | Magnesium electrolysis chlorine gas purification process |
-
2018
- 2018-04-26 CN CN201820611355.8U patent/CN208372763U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112387050A (en) * | 2020-11-13 | 2021-02-23 | 攀枝花钢企欣宇化工有限公司 | Magnesium electrolysis chlorine gas purification process |
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