CN206604474U - The dustless Cosmetic material system of powder catalyst - Google Patents
The dustless Cosmetic material system of powder catalyst Download PDFInfo
- Publication number
- CN206604474U CN206604474U CN201720098614.7U CN201720098614U CN206604474U CN 206604474 U CN206604474 U CN 206604474U CN 201720098614 U CN201720098614 U CN 201720098614U CN 206604474 U CN206604474 U CN 206604474U
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- Prior art keywords
- catalyst
- closed
- dustless
- material system
- cosmetic material
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- 239000003054 catalyst Substances 0.000 title claims abstract description 110
- 239000000843 powder Substances 0.000 title claims abstract description 47
- 239000000463 material Substances 0.000 title claims abstract description 24
- 239000002537 cosmetic Substances 0.000 title claims abstract description 23
- 238000003860 storage Methods 0.000 claims abstract description 29
- 239000000428 dust Substances 0.000 claims abstract description 26
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 23
- 238000005243 fluidization Methods 0.000 claims abstract description 20
- 238000000746 purification Methods 0.000 claims abstract description 14
- 238000011084 recovery Methods 0.000 claims abstract description 13
- 230000000630 rising effect Effects 0.000 claims 1
- 238000000034 method Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000006555 catalytic reaction Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
The utility model is related to a kind of dustless Cosmetic material system of powder catalyst.The dustless Cosmetic material system of the powder catalyst is closed into warehouse receipt member and dust purification recovery unit including new agent；New agent, which is closed into warehouse receipt member, includes closed bale breaker and fluidisation distributor, the feed end of the discharge end connection fluidisation distributor of closed bale breaker, the discharge end connection fresh catalyst storage tank of fluidisation distributor；Dust purification recovery unit includes cyclone separator and deduster, the inlet end connection fresh catalyst storage tank of cyclone separator, the outlet side of cyclone separator connects the inlet end of deduster, and the exhaust end of cyclone separator and the exhaust end of deduster connect fresh catalyst storage tank respectively.The dustless Cosmetic material system of the powder catalyst, it is closed to the progress of powder catalyst to unpack, fluidize conveying, pollution of the dust to air is reduced, and powder catalyst can be reclaimed, without artificial operation, operating efficiency is high.
Description
Technical field
The utility model is related to technical field of catalyst treatment, more particularly to a kind of dustless Cosmetic material system of powder catalyst
System.
Background technology
In the production process in general chemical plant, often it may require that using substantial amounts of catalyst come catalytic reaction thing, so that
Chemical reaction can be favorably accomplished, and increase the production efficiency of product.In order to improve the catalytic effect of catalyst, raising is urged
Agent and reaction mass contact area, many catalyst are fabricated to particle and powder morphology, and such as FCC apparatus and MTO devices are urged
Agent is tiny spheric granules, and particle diameter is typically at 20-100 μm.
Greatly, and catalyst is using can gradually lose effect of catalysis after a period of time for catalyst amount, it is therefore necessary to
The catalyst often more to renew.During transport, more catalyst changeout, powder catalyst is easy to leak to working environment
In, the pollution of environment is in turn resulted in, and the health and safety of operating personnel can be influenceed.
The tradition charging flow of powder catalyst is as follows：Fresh catalyst by tank car in bulk, container-type car or truck,
Transported from catalyst plant to catalytic cracking unit, by manually by catalyst unpacking, pouring into blowpit, then pass through vacuum handling
System transfer is to new agent tank.
Traditional charging process has that environment dust pollution is big, operator in artificial unpacking and new agent tank tank deck exhaust process
Member must execute-in-place, hand labor intensity is big, operating environment is poor, efficiency is low, catalyst loss is big, catalyst exposed air
Catalyst after time length, the easy moisture absorption, the moisture absorption, which enters in reaction unit, easily to be produced thermal runaway, catalyst activity reduction and asks
Topic.
Therefore, a kind of automation of offer, the charging system of dustlessization are needed badly, to solve prior art powder catalyst charge
During dust pollution is serious, catalyst loss big, manual site's inefficient operation the problem of.
Utility model content
(1) technical problem to be solved
In order to solve the above mentioned problem of prior art, the utility model provides one kind and closed can unpack, fluidizes conveying, simultaneously
The dustless Cosmetic material system of powder catalyst that powder catalyst can be reclaimed.
(2) technical scheme
In order to achieve the above object, the main technical schemes that the utility model is used include：
The utility model provides a kind of dustless Cosmetic material system of powder catalyst, including new agent is closed into warehouse receipt member and dust
Recovery Purifying unit；New agent, which is closed into warehouse receipt member, includes closed bale breaker, fluidisation distributor and fresh packed catalyst, closed to tear open
Bag device is provided with feed end and discharge end, and fluidisation distributor is provided with feed end and discharge end, and the feed end connection of closed bale breaker is new
Fresh packed catalyst, the feed end of the discharge end connection fluidisation distributor of closed bale breaker, the discharge end connection of fluidisation distributor
Fresh catalyst storage tank；Dust purification recovery unit includes cyclone separator and deduster, cyclone separator provided with inlet end and
Outlet side, deduster is provided with inlet end and outlet side, the inlet end connection fresh catalyst storage tank of cyclone separator, cyclonic separation
The outlet side of device connects the inlet end of deduster.
According to the utility model, cyclone separator and deduster are additionally provided with exhaust end, the exhaust end of cyclone separator and remove
The exhaust end of dirt device connects fresh catalyst storage tank respectively.
According to the utility model, fresh catalyst storage tank is true provided with one with fluidizing the port that the discharge end of distributor is connected
Empty delivery pump.
According to the utility model, first filter core is set on the side wall of closed bale breaker, the first filter core is unpacked with closed
Device pipeline is connected.
According to the utility model, the feed end of closed bale breaker sets double-deck barrel.
According to the utility model, the first valve is set between the exhaust end and fresh catalyst storage tank of cyclone separator, removed
The second valve is set between the exhaust end and fresh catalyst storage tank of dirt device.
According to the utility model, new agent, which is closed into warehouse receipt member, also includes a lifting for being used to transport fresh packed catalyst
Equipment.
According to the utility model, crane gear is electric hoist.
According to the utility model, the second filter core is provided with deduster, the second filter core top is air-purifying chamber.
According to the utility model, the outlet side of deduster is connected with air-purifying chamber.
(3) beneficial effect
The beneficial effects of the utility model are：The dustless Cosmetic material system of powder catalyst that the utility model is provided, changes
The pattern of prior art powder catalyst hand charging, without artificial operation, while dress agent and dedusting are combined, is realized
It is closed to the progress of powder catalyst to unpack, fluidize conveying, and powder catalyst can be reclaimed, reduce powder catalysis
The loss of agent, the clean gas dust content after purification is less than 10mg/m3, the pollution to environment is reduced, work is improved
Make efficiency.
Brief description of the drawings
Fig. 1 is the schematic diagram of the dustless Cosmetic material system of powder catalyst；
Fig. 2 is the flow chart that new agent is closed into warehouse receipt member；
Fig. 3 is the flow chart of dust purification recovery unit.
【Description of reference numerals】
1：Closed bale breaker；2：Fluidize distributor；3：Fresh catalyst storage tank；4：Cyclone separator；5：Deduster；6：Rise
Heavy equipment；7：Fresh packed catalyst；8：Double-deck barrel；9：First filter core；16：Air-purifying chamber；17：First valve；18：Second valve
Door；19：Second filter core；20：Vacuum handling pump；100：New agent is closed into warehouse receipt member；200：Dust purification recovery unit.
Embodiment
It is below in conjunction with the accompanying drawings, right by embodiment in order to understand in order to preferably explain the utility model
The utility model is described in detail.
Embodiment one
The utility model provides a kind of dustless Cosmetic material system of powder catalyst, including new agent is closed into first 100 Hes of warehouse receipt
Dust purification recovery unit 200.
Reference picture 1, new agent, which is closed into warehouse receipt member 100, includes closed bale breaker 1, fluidisation distributor 2 and fresh packed catalysis
Agent 7, closed bale breaker 1 is provided with feed end and discharge end, and fluidisation distributor 2 is provided with feed end and discharge end, closed bale breaker 1
Feed end connects fresh packed catalyst 7, the feed end of the discharge end connection fluidisation distributor 2 of closed bale breaker 1, fluidisation distribution
The discharge end connection fresh catalyst storage tank 3 of device 2.
Specifically, fresh catalyst storage tank 3 is provided with a vacuum handling with fluidizing the port that the discharge end of distributor 2 is connected
Pump 20, for the catalyst transport in distributor 2 will to be fluidized in fresh catalyst storage tank 3, because vacuum handling pump 20 is powerful
Swabbing action, do not result in line clogging., it is necessary to which the gas of generation is discharged during powder catalyst loading and unloading.By
Contain a small amount of catalyst dust in exhaust, it is impossible to be expelled directly out, therefore set on the side wall of closed bale breaker 1 by pipeline
First filter core 9 is put, the catalyst dust mixed in exhaust so can have both been filtered out, the purpose of exhaust can be reached again.
The feed end of closed bale breaker 1 sets double-deck barrel 8 so that fresh packed catalyst 7 is more encrypted when being contacted with closed bale breaker 1
Close, prevent dust from overflowing.
Further, new agent, which is closed into warehouse receipt member 100, also includes a crane gear for being used to transport fresh packed catalyst 7
6, the top for fresh packed catalyst 7 to be delivered to closed bale breaker 1.In the utility model embodiment, this resets
Standby 6 be electric hoist, but for the utility model, it is not limited to this or other have what improving material was acted on
Device.
Reference picture 1, dust purification recovery unit 200 include cyclone separator 4 and deduster 5, cyclone separator 4 be provided with into
Gas end and outlet side, deduster 5 are provided with inlet end and outlet side, the inlet end connection fresh catalyst storage tank of cyclone separator 4
3, the outlet side of cyclone separator 4 connects the inlet end of deduster 5.
Further, cyclone separator 4 and deduster 5 further respectively have exhaust end, the exhaust end of cyclone separator 4 and dedusting
The exhaust end of device 5 connects fresh catalyst storage tank 3 respectively.The exhaust end of cyclone separator 4 and the exhaust end of deduster 5 can be received
Collection storage plays a part of recovery by cyclone separator 4 and the fresh catalyst of the separating and filtering of deduster 5.
Specifically, first valve 17 is set between the exhaust end of cyclone separator 4 and fresh catalyst storage tank 3, removed
One the second valve 18 is set between the exhaust end and fresh catalyst storage tank 3 of dirt device 5.Enter the mistake of luggage agent in powder catalyst
Cheng Zhong, the first valve 17 and the second valve 18 are closed, after dress agent process terminates, then by the first valve 17 and the second valve 18
Open, the fresh powder catalyst that sedimentation filtration is obtained in cyclone separator 4 and deduster 5 can thus be reclaimed and entered
In fresh catalyst storage tank 3, without extra conveying and power, simple to operate, the saving energy.
Further, cyclone separator 4 can separate >=10 μm of solid particle, and deduster 5 can filter≤1 μm of solid
Particle.
Further, it is less than 10mg/m by the dustiness of the purified gas of dust purification recovery unit 2003。
Embodiment two
The operating process of the dustless Cosmetic material system of powder catalyst that the utility model is provided is：
Referring to Figures 1 and 2, new agent is closed into warehouse receipt member 100, is delivered to fresh packed catalyst 7 by electric hoist closed
Between the top of bale breaker 1, the double-deck barrel 8 for the feed end that the sack of fresh packed catalyst 7 is filled in into closed bale breaker 1.Put
Put it is safe after the cover with sealing ring is fixed to the sack of fresh packed catalyst 7, solve opened mouth tether, fresh catalyst
Enter fluidisation distributor 2 after closed bale breaker 1, while being passed through air to fluidisation distributor 2, fresh catalyst is in fluidisation point
It is delivered to after being mixed in cloth device 2 with Air Fluidized by vacuum handling pump 20 in fresh catalyst storage tank 3.Powder catalyst is close
After the dust-laden exhaust produced during unpacking is closed via the first filter core 9 filtering of closed bale breaker 1, the gas of purification is arranged
To air, dust pollution air is prevented.
Wherein, the concentration of powder catalyst is very big, and it can realize powder by fluidizing the fluidisation distribution grid of distributor 2
Gas-solid mixing is fluidized, and does not result in blocking.
In reference picture 1 and Fig. 3, dust purification recovery unit 200, the dust laden air in fresh catalyst storage tank 3 leads to first
The inlet end for crossing cyclone separator 4 enters in cyclone separator 4, and particle larger in dust laden air is removed, removed out
The a small amount of dust catalyst sedimentation come is to the exhaust end of cyclone separator 4, and the gas after the removing of cyclone separator 4, which passes through, to be revolved
The outlet side of wind separator 4 enters the inlet end of deduster 5, carries out mixing in further dedusting, gas hence into deduster 5
Dust catalyst be intercepted and be attached to the outer surface of the second filter core 19, the clean gas dust content after purification is less than
10mg/m3, then the air-purifying chamber 16 that the second filter core 19 enters deduster 5 is passed through, then arranged from the outlet side of deduster 5 to air.
Cyclone separator 4 can be with automatic running, and without operation and maintenance, deduster 5 needs regularly blowback, by supporting control system
Automatic running, detailed process is：Injection pipeline opening is periodically opened, blast pass enters from the openend of the second filter core 19, and passes through
The second outwards flowing of filter core 19, powder catalyst is got off to the exhaust end of deduster 5 from the outer surface blowback of the second filter core 19.Beat
The first valve 17 and the second valve 18 are opened, the powder being stored in the exhaust end of the exhaust end of cyclone separator 4 and deduster 5 is urged
Agent is settled downwards and fallen into fresh catalyst storage tank 3 under gravity, reaches the purpose that catalyst is reclaimed.Thus,
Reclaiming the powder catalyst of filtering can directly drain into fresh catalyst storage tank 3, without extra conveying equipment and power.
In summary, the dustless Cosmetic material system of powder catalyst that the utility model is provided, changes prior art powder
The pattern of catalyst hand charging, without artificial operation, while dress agent and dedusting are combined, realize and powder catalyst is entered
Row is closed to be unpacked, fluidizes conveying, and powder catalyst can be reclaimed, and reduces the loss of powder catalyst, is passed through
Clean gas dust content after purification is less than 10mg/m3, the pollution to environment is reduced, operating efficiency is improved.
It is to be appreciated that the description carried out above to specific embodiment of the utility model is simply to illustrate that this practicality
New technology path and feature, its object is to allow those skilled in the art to understand content of the present utility model simultaneously
Implement according to this, but the utility model is not limited to above-mentioned particular implementation.Every scope in the utility model claim
The various change inside made or modification, should all cover in protection domain of the present utility model.
Claims (10)
1. a kind of dustless Cosmetic material system of powder catalyst, it is characterised in that：Warehouse receipt first (100) and dust are closed into including new agent
Recovery Purifying unit (200)；
Described new dose is closed into warehouse receipt first (100) and includes closed bale breaker (1), fluidisation distributor (2) and fresh packed catalyst
(7), the closed bale breaker (1) is provided with feed end and discharge end, and the fluidisation distributor (2) is provided with feed end and discharge end,
The feed end of the closed bale breaker (1) connects fresh packed catalyst (7), the discharge end connection of the closed bale breaker (1)
The feed end of the fluidisation distributor (2), the discharge end connection fresh catalyst storage tank (3) of the fluidisation distributor (2)；
The dust purification recovery unit (200) includes cyclone separator (4) and deduster (5), and the cyclone separator (4) sets
There are inlet end and outlet side, the deduster (5) is provided with inlet end and outlet side, and the inlet end of the cyclone separator (4) connects
The fresh catalyst storage tank (3) is connect, the outlet side of the cyclone separator (4) connects the inlet end of the deduster (5).
2. the dustless Cosmetic material system of powder catalyst as claimed in claim 1, it is characterised in that：
The cyclone separator (4) and the deduster (5) are additionally provided with exhaust end, the exhaust end of the cyclone separator (4) and
The exhaust end of the deduster (5) connects the fresh catalyst storage tank (3) respectively.
3. the dustless Cosmetic material system of powder catalyst as claimed in claim 1, it is characterised in that：
The port that the fresh catalyst storage tank (3) is connected with the discharge end of the fluidisation distributor (2) is defeated provided with a vacuum
Send pump (20).
4. the dustless Cosmetic material system of powder catalyst as claimed in claim 1, it is characterised in that：
One the first filter core (9) is set on the side wall of the closed bale breaker (1), and first filter core (9) closed is torn open with described
Bag device (1) pipeline is connected.
5. the dustless Cosmetic material system of powder catalyst as claimed in claim 1, it is characterised in that：
The feed end of the closed bale breaker (1) sets double-deck barrel (8).
6. the dustless Cosmetic material system of powder catalyst as claimed in claim 2, it is characterised in that：
The first valve (17) is set between the exhaust end and the fresh catalyst storage tank (3) of the cyclone separator (4), it is described
Second valve (18) is set between the exhaust end of deduster (5) and the fresh catalyst storage tank (3).
7. the dustless Cosmetic material system of powder catalyst as described in claim any one of 1-6, it is characterised in that：
Described new dose is closed into warehouse receipt first (100) and is also reseted including one for transporting rising for the fresh packed catalyst (7)
Standby (6).
8. the dustless Cosmetic material system of powder catalyst as claimed in claim 7, it is characterised in that：
The crane gear (6) is electric hoist.
9. the dustless Cosmetic material system of powder catalyst as claimed in claim 8, it is characterised in that：
The second filter core (19) is provided with the deduster (5), the second filter core (19) top is air-purifying chamber (16).
10. the dustless Cosmetic material system of powder catalyst as claimed in claim 9, it is characterised in that：
The outlet side of the deduster (5) is connected with air-purifying chamber (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720098614.7U CN206604474U (en) | 2017-01-26 | 2017-01-26 | The dustless Cosmetic material system of powder catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720098614.7U CN206604474U (en) | 2017-01-26 | 2017-01-26 | The dustless Cosmetic material system of powder catalyst |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206604474U true CN206604474U (en) | 2017-11-03 |
Family
ID=60167895
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720098614.7U Expired - Fee Related CN206604474U (en) | 2017-01-26 | 2017-01-26 | The dustless Cosmetic material system of powder catalyst |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206604474U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112495311A (en) * | 2020-10-13 | 2021-03-16 | 新疆中泰化学股份有限公司 | Low-mercury catalyst three-turn method and device |
-
2017
- 2017-01-26 CN CN201720098614.7U patent/CN206604474U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112495311A (en) * | 2020-10-13 | 2021-03-16 | 新疆中泰化学股份有限公司 | Low-mercury catalyst three-turn method and device |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171103 |