CN108839285A - Scrap rubber system of processing - Google Patents
Scrap rubber system of processing Download PDFInfo
- Publication number
- CN108839285A CN108839285A CN201810566839.XA CN201810566839A CN108839285A CN 108839285 A CN108839285 A CN 108839285A CN 201810566839 A CN201810566839 A CN 201810566839A CN 108839285 A CN108839285 A CN 108839285A
- Authority
- CN
- China
- Prior art keywords
- expansion chamber
- outlet tube
- cabinet
- separating mechanism
- scrap rubber
- 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.)
- Withdrawn
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/04—Disintegrating plastics, e.g. by milling
- B29B17/0412—Disintegrating plastics, e.g. by milling to large particles, e.g. beads, granules, flakes, slices
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/04—Disintegrating plastics, e.g. by milling
- B29B2017/0424—Specific disintegrating techniques; devices therefor
- B29B2017/0484—Grinding tools, roller mills or disc mills
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a kind of scrap rubber systems of processing, including the first cabinet, the second cabinet, the expansion chamber on rear side of the second cabinet and the hothouse on rear side of the expansion chamber, second bottom of box is equipped with outlet tube, the outlet tube is connected with the medium position of the expansion chamber, the expansion chamber top is equipped with clear liquid outlet pipe, expansion chamber lower part is equipped with mixed liquid outlet tube, which is connected with the hothouse;Pass through the setting of outlet tube, it is precipitated in order to which mixed liquor is discharged into expansion chamber, after a period of time, clear liquid is discharged into hothouse from mixed liquid outlet tube from the clear liquid water outlet discharge above expansion chamber, mixed liquid, reduce the content of moisture, in order to more effectively be dried, dry speed is accelerated, simultaneously, clear liquid can be utilized again, save water resource.
Description
Technical field
The invention belongs to rubber dust treatment device technical fields, more particularly, to a kind of scrap rubber system of processing.
Background technique
Scrap rubber usually needs to be recycled after over cleaning, drying, broken, reconstruction are at processes such as particles, therefore
It needs to carry out pulverization process to scrap rubber when recycling scrap rubber.
Existing scrap rubber crusher can generate a large amount of rubber powder dust when to rubber pulverizing, and rubber powder dust be easy it is quick-fried
It is fried, can be to avoid explosion so need to be drenched with water, but persistently conveying water is drenched, it wastes water very much and mixed liquor
In moisture content it is very more, be unfavorable for rapid draing.
Summary of the invention
The present invention for overcome the deficiencies in the prior art, provides a kind of scrap rubber system of processing that rate of drying is fast.
To achieve the goals above, the present invention uses following technical scheme:A kind of scrap rubber system of processing, including the first case
Body, the second cabinet, the expansion chamber on rear side of the second cabinet and the hothouse on rear side of the expansion chamber, second cabinet bottom
Portion is equipped with outlet tube, which is connected with the medium position of the expansion chamber, and the expansion chamber top is discharged equipped with clear liquid
Pipe, expansion chamber lower part are equipped with mixed liquid outlet tube, which is connected with the hothouse;By the setting of outlet tube, with
It is precipitated convenient for mixed liquor is discharged into expansion chamber, after a period of time, clear liquid is mixed from the clear liquid water outlet discharge above expansion chamber
Liquid is discharged into hothouse from mixed liquid outlet tube, reduces the content of moisture, in order to more effectively be dried, accelerates drying
Speed, meanwhile, clear liquid can be utilized again, save water resource.
The hothouse include tank body, the fog-spray nozzle set on tank body top, the air inlet pipe set on tank body lower part and with this into
The jet thrust that tracheae is connected;The mixed liquid outlet tube is connected with the fog-spray nozzle;Setting using the above structure, hothouse can
Being sprayed of being formed of rubber powder liquid to be dried by all parts, and by hot gas to spraying carry out jet drying, quickening
The speed of spray drying improves the efficiency of rubber powder extraction.
Crushing mechanism and the first separating mechanism are equipped in first cabinet, the crushing mechanism includes for grinding rubber
The water sprinkler to roller and two relative tilts, the clear liquid outlet pipe is connected with the water sprinkler;By the setting to roller,
Scrap rubber block can be crushed, it is made to become graininess, in order to subsequent utilization, while water sprinkler is used for scrap rubber
The rubber powder generated when broken is drenched, and rubber powder is avoided to wave everywhere, and leads to dangerous generation, improves the safety of rubber powder processing
Property.
The outlet tube end stretches in the expansion chamber, and is connected with baffle cover;By the setting of above structure, make
Mixed liquor can be delivered into expansion chamber and be precipitated, avoid water flow from causing to rush to the rubber powder precipitated in expansion chamber when intaking
It hits, and clear liquid and mixed liquid is caused to mix again, influence the efficiency of precipitating.
The baffle cover is connected by multiple connection straps with the outlet tube, and the opening of the baffle cover is towards the outlet tube
With the junction of expansion chamber;By the setting of connection strap, fixed effect is played to baffle cover, reinforce outlet tube and baffle cover it
Between structural stability, while the setting of baffle cover opening improves the efficiency of conveying in order to which baffle cover transfers out mixed liquid.
The second separating mechanism and third separating mechanism are equipped in second cabinet, the crushing mechanism is set to the first separation
The top of mechanism, second separating mechanism are set to the top of third separating mechanism;First separating mechanism, the second separating mechanism and
The dust that third separating mechanism is used to be dissolved in water carries out flocculation treatment, in order to which the impurity such as dust in dust are separated, with
It is convenient for the subsequent recycling to rubber powder, by the setting of above structure, the impurity such as rubber powder and dust are carried out
Thoroughly separation, in order to be recycled to rubber powder, substantially increases the efficiency of separation.
First separating mechanism includes multiple the first Flocculent plate and the first filter screen being equidistantly staggered, and described first
Filter screen is set to the side of the first Flocculent plate;By the setting of the first Flocculent plate, can wad a quilt with cotton to the mixing liquid flow down
The impurity reactions such as dust in mixing liquid are generated flocculation, are then filtered by the first filter screen by solidifying processing, from
And flocculation is isolated, in order to recycle rubber powder, improve separative efficiency.
Second separating mechanism includes flocculation pipeline and the second filter screen, and the flocculation pipeline is set on the second filter screen
Side;By the setting for the pipeline that flocculates, allow mixing liquid by secondary flocculation treatment, in order to more thoroughly separate mixing
Dust in liquid is separated flocculation by the filtering of the second filter screen, so that isolated effect is more preferable.
The present invention has the following advantages that:This scrap rubber system of processing hothouse expansion chamber made above setting, so as to
It is precipitated in rubber powder mixed liquor, to be divided into clear liquid and mixed liquid, clear liquid is conveyed into water sprinkler and carries out repetitive cycling
It uses, water resource is saved, while the moisture content in mixed liquid reduces very much, in order to quickly be done into hothouse
It is dry, substantially increase dry efficiency.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is the schematic enlarged-scale view at the B in Fig. 1.
Fig. 3 is the structural schematic diagram of the hothouse in Fig. 1.
Fig. 4 is the schematic enlarged-scale view at the A in Fig. 3.
Fig. 5 is the first Flocculent plate structural schematic diagram of Fig. 1.
Fig. 6 is the second Flocculent plate structural schematic diagram of Fig. 1.
Specific embodiment
In order to make those skilled in the art better understand the present invention program, below in conjunction in the embodiment of the present invention
Attached drawing, the technical scheme in the embodiment of the invention is clearly and completely described, it is clear that described embodiment is only
A part of the embodiments of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, ordinary skill people
The model that the present invention protects all should belong in member's every other embodiment obtained without making creative work
It encloses.
As shown in Figure 1, as shown in Figure 1-3, a kind of scrap rubber regenerates system of processing, including the first cabinet 1 and the second cabinet
2, be equipped with crushing mechanism and the first separating mechanism in first cabinet 1, be equipped in second cabinet 2 second separating mechanism and
Third separating mechanism, the crushing mechanism are set to the top of the first separating mechanism, and second separating mechanism is separated set on third
The top of mechanism, crushing mechanism is for being ground scrap rubber fragment, in order to which scrap rubber is crushed, formation
Grain, the dust that the first separating mechanism, the second separating mechanism and third separating mechanism are used to be dissolved in water carry out flocculation treatment, so as to
It is separated in by impurity such as dusts in dust, in order to carry out the subsequent recycling to rubber powder, by the setting of above structure,
The impurity such as rubber powder and dust are thoroughly separated, in order to be recycled to rubber powder, are substantially increased point
From efficiency.
The crushing mechanism includes the water sprinkler 32 to roller 31 and two relative tilts for grinding rubber, the watering
Device 32 is set on 1 roof of cabinet, and connects external water sending device, described to pass through motor driven to roller 31, connects the output of motor
Axis, the motor are set on cabinet 1, and the water sprinkler 32 is set to can be right by the setting to roller 31 to the top of roller 31
Scrap rubber block is crushed, it is made to become graininess, in order to subsequent utilization, while water sprinkler 32, for broken to scrap rubber
The rubber powder generated when broken is drenched, and rubber powder is avoided to wave everywhere, and leads to dangerous generation, improves the safety of rubber powder processing
Property;It is described to offering feed inlet 33 above roller 31, it is described to be equipped with the breaking disc 311 being equidistantly staggered to roller 31, it is described
To roller 31 include two breaker rolls, the breaker roll by breaking disc 311 staggeredly is engaged, scrap rubber fragment can by into
Material mouth 33 is fallen on on roller 31, and in order to directly carry out pulverization process to roller 31, the setting of breaking disc 33 is accelerated broken to roller
The speed of 31 broken scrap rubber fragments, improves the efficiency of crushing.
First separating mechanism includes multiple the first Flocculent plate 41 and the first filter screen 42 being equidistantly staggered, described
First filter screen, 42 one end is set to the side of the first Flocculent plate 41, and 42 other end of the first filter screen connects the tank wall of cabinet 1,
Described first Flocculent plate, 41 one end connects 1 side wall of cabinet, and 41 other end of the first Flocculent plate is vacantly arranged, and the first Flocculent plate
41 tilt down towards hanging direction, by the setting of the first Flocculent plate 41, can flocculate to the mixing liquid flow down
The reaction of the impurity such as dust in mixing liquid is generated flocculation, is then filtered by the first filter screen 42 by processing, from
And flocculation is isolated, in order to recycle rubber powder, improve separative efficiency;It is equidistantly equipped at intervals on first Flocculent plate 41
Horizontally disposed first flocculation tank 411 in bottom surface, the junction between first flocculation tank 411 is arc-shaped protrusions shape, and bottom surface is
It is horizontally disposed, in order to which water flow can be directly from bottom surface quickly through and being set as the junction between the first flocculation tank 411
Arcuation can flow directly into the first flocculation tank 411 in order to which mixing liquid is fallen on arcuation bump, very convenient, pass through
The setting of first flocculation tank 411, so that water flow can flocculate during flowing, in order to wad a quilt with cotton faster
It is solidifying, improve flocculated efficiency.
The third separating mechanism includes flocculation pedestal 61 and third filter screen 62, and the third filter screen 62 is set to second
On the tank wall of cabinet 2, the direction of flocculation pedestal 61 towards the third filter screen 62 is obliquely installed, and the third filter screen 62 is logical
By the setting for the pedestal 61 that flocculates rubber powder mixing liquid after flocculation is flowed to by flocculation pedestal 61 to external pipe
Third filter screen 62 can thoroughly separate the impurity such as the dust in the remittance of rubber powder mixed liquor, then to filter out flocculation
Rubber powder can be extracted, be recycled;The second Flocculent plate 63, second Flocculent plate are equipped with above the flocculation pedestal 61
Multiple second flocculation tanks 412, the structure of the structure of second Flocculent plate 63 and the first Flocculent plate 41 are equidistantly equipped at intervals on 63
It is identical, by the setting of the second Flocculent plate 63, flocculation reaction can be carried out to mixing liquid again, in order to more thoroughly will
The impurity such as the dust in mixing liquid are separated, so as to so that the big equal impurity of dust in mixing liquid are completely separated out
It goes, in order to recycle rubber powder;Multiple baffles 412, the baffle 412 are equidistantly equipped at intervals on first flocculation tank, 411 side wall
Gap is equipped between bottom surface, the baffle 412 has one end to be vacantly arranged, and the other end connects the inner wall of the first flocculation tank 411, leads to
The setting for crossing baffle 412, allows mixing liquid in flow process, the space formed between baffle 412 and baffle 412
The small vortex of interior progress accelerates flocculated speed, while the setting in gap in order to reduce the flocculated time, can will wad a quilt with cotton
Product after solidifying by gap as water flow washes away, to accelerate the efficiency of separation.
Second separating mechanism includes flocculation pipeline 51 and the second filter screen 52, and the flocculation pipeline 51 is set to the second mistake
52 top of strainer, the flocculation pipeline 51 is S-shaped to be bent downwardly setting, and the outlet of flocculation pipeline 51 is set to the second filter screen 52
Top, second filter screen 52 tilts down setting, by the setting for the pipeline 51 that flocculates, mixing liquid is passed through
Secondary flocculation treatment, in order to which the dust in more thorough separating mixed liquids will be flocculated by the filtering of the second filter screen 52
Product is separated, so that isolated effect is more preferable;The flocculation pipeline 51 is equipped with admission chamber 511 and multiple equidistant intervals are set
The fluid hole 512 set, the fluid hole 512 is obliquely installed towards the opposite direction of water flow, in order to which flocculant pours mixed liquor
It in body, quickly incorporates in mixing liquid, is quickly flocculated, accelerate the speed dissolved, by the setting of admission chamber 511,
Flocculant can be passed through in flocculation pipeline 51, to be flowed out from fluid hole 512, be passed through in mixing liquid and flocculate, make
Obtaining mixing liquid can flocculate during flowing, improve flocculated efficiency, accelerate the speed of separation.
The expansion chamber 8 is set to 2 rear side of the second cabinet, and 2 bottom of the second cabinet is equipped with outlet tube 21, the outlet tube 21
It is connected with the medium position of the expansion chamber 8;8 top of expansion chamber is equipped with clear liquid outlet pipe 81, and 8 lower part of expansion chamber is equipped with
Mixed liquid outlet tube 82, the mixed liquid outlet tube 82 are connected with the hothouse 7, by the setting of outlet tube, in order to by mixed liquor
It is discharged into expansion chamber 8 to be precipitated, after a period of time, clear liquid is discharged from the clear liquid water outlet 81 above expansion chamber 8, mixes liquid from mixed liquid
It is discharged into hothouse 7 in outlet tube 82, reduces the content of moisture, in order to more effectively be dried, accelerates dry speed
Degree, meanwhile, clear liquid can be utilized again, save water resource;21 end of outlet tube stretches to the expansion chamber 8
It is interior, and it is connected with baffle cover 83, by the setting of above structure, mixed liquor is delivered into expansion chamber 8 and is sunk
It forms sediment, water flow is avoided to cause to impact to the rubber powder precipitated in expansion chamber 8 when intaking, and clear liquid and mixed liquid is caused to be blended in one again
It rises, influences the efficiency of precipitating;The baffle cover 83 is connected by multiple connection straps 84 with the outlet tube 21, the baffle cover 83
Opening fixation is played to baffle cover 83 by the setting of connection strap 84 towards the outlet tube 21 and the junction of expansion chamber 8
Effect, reinforce the structural stability between outlet tube 21 and baffle cover 83, while the setting that baffle cover 83 is open, in order to
Baffle cover 83 transfers out mixed liquid, improves the efficiency of conveying.
The hothouse 7 is set to the rear side of expansion chamber 8, the hothouse 7 include inner tank body 71, outer tank body 72, formed with it is interior
Cavity 73 between outer tank body, set on tank body top inlet tube 74, be connected with the inlet tube 74 aerosolizing part, with the sky
The air inlet pipe 75 that chamber 73 is connected and the multiple groups fumarole group in inner tank body 72, setting using the above structure, hothouse
7 can be dried being sprayed of being formed of rubber powder liquid by all parts, and be added by hot gas to spraying carry out jet drying
The fast speed of spray drying, improves the efficiency of rubber powder extraction, is equipped with spiral helicine heating tube 731 in the cavity 73, leads to
It crosses and spiral helicine setting is carried out to heating tube 731, increase the area of heat diffusion, improve the efficiency of heating, so that hot gas
The speed of generation is faster.
The multiple groups fumarole group evenly spaced distribution along the length direction of the inner tank body 71, every group of fumarole
Group includes multiple fumaroles 711 along the circumferentially-spaced distribution of 71 inner wall of inner tank body, and the fumarole 711 is by down toward updip
Tiltedly setting allows the hot gas in cavity 73 along fumarole 711 by carrying out the setting of fumarole 711 to fumarole group
It ejects, in order to being dried by spraying, while to the inclined setting of fumarole 711, allows hot gas against spraying
It is sprayed, accelerates the efficiency of spray drying, be evenly distributed with multiple lug bosses 791, lug boss on 79 inner wall of spray orifice
791 setting improves so that water energy is enough to hit with lug boss 791, and then enhances atomizing effect when spray orifice 79 to water spray
The efficiency of later period drying.
The aerosolizing part includes the storage liquid pipe 76 being connected with the inlet tube, rotatable disturbing in storage liquid pipe
Stream part 77, the spray head 78 being connected with the storage liquid pipe and multiple spray orifices 79 on spray head, the structure of spoiler 77 and waterwheel
It is similar, and can be rotated under motor driven, to stir the liquid stored in liquid pipe 76, guarantees that rubber powder is blended in always and store liquid pipe 76
Water in, avoid rubber powder deposit and block spray orifice 79, can be more effectively sprayed, substantially increase the effect of spray injection
Rate.
Claims (8)
1. a kind of scrap rubber system of processing, including the first cabinet(1), the second cabinet(2), expansion chamber on rear side of the second cabinet
(8)And it is set to the expansion chamber(8)The hothouse of rear side(7);It is characterized in that:Second cabinet(2)Bottom is equipped with outlet tube
(21), the outlet tube(21)With the expansion chamber(8)Medium position be connected, the expansion chamber(8)Top goes out equipped with clear liquid
Water pipe(81), expansion chamber lower part is equipped with mixed liquid outlet tube(82), the mixed liquid outlet tube(82)With the hothouse(7)It is connected.
2. scrap rubber system of processing according to claim 1, it is characterised in that:The hothouse includes tank body(71), set
Fog-spray nozzle in tank body top(72), set on the air inlet pipe of tank body lower part(73)And the jet thrust being connected with the air inlet pipe
(74);The mixed liquid outlet tube(82)With the fog-spray nozzle(72)It is connected.
3. scrap rubber system of processing according to claim 1, it is characterised in that:First cabinet(1)Interior be equipped with is crushed
Mechanism and the first separating mechanism, the crushing mechanism include for grind rubber to roller(31)With the watering of two relative tilts
Device(32), the clear liquid outlet pipe(81)With the water sprinkler(32)It is connected.
4. scrap rubber system of processing according to claim 1, it is characterised in that:The outlet tube(21)End stretches to institute
State expansion chamber(8)It is interior, and it is connected with baffle cover(83).
5. scrap rubber system of processing according to claim 1, it is characterised in that:The baffle cover(83)Pass through multiple connections
Item(84)With the outlet tube(21)It is connected, the baffle cover(83)Opening towards the outlet tube(21)With expansion chamber(8)'s
Junction.
6. scrap rubber system of processing according to claim 1, it is characterised in that:Second cabinet(2)Inside it is equipped with second
Separating mechanism and third separating mechanism, the crushing mechanism are set to the top of the first separating mechanism, and second separating mechanism is set
In the top of third separating mechanism.
7. scrap rubber system of processing according to claim 6, it is characterised in that:First separating mechanism includes multiple etc.
Away from the first Flocculent plate being staggered(41)With the first filter screen(42), first filter screen(42)Set on the first Flocculent plate
(41)Side.
8. scrap rubber system of processing according to claim 7, it is characterised in that:Second separating mechanism includes flocculation pipe
Road(51)With the second filter screen(52), the flocculation pipeline(51)Set on the second filter screen(52)Top.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201810566839.XA CN108839285A (en) | 2018-06-05 | 2018-06-05 | Scrap rubber system of processing |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810566839.XA CN108839285A (en) | 2018-06-05 | 2018-06-05 | Scrap rubber system of processing |
Publications (1)
Publication Number | Publication Date |
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CN108839285A true CN108839285A (en) | 2018-11-20 |
Family
ID=64210625
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201810566839.XA Withdrawn CN108839285A (en) | 2018-06-05 | 2018-06-05 | Scrap rubber system of processing |
Country Status (1)
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CN (1) | CN108839285A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112140493A (en) * | 2020-09-03 | 2020-12-29 | 南通顺驰橡胶制品有限公司 | Production process for preparing new butyl rubber inner tube by utilizing waste butyl rubber inner tube |
CN113666532A (en) * | 2021-08-09 | 2021-11-19 | 滁州永强汽车制造有限公司 | Flocculation sedimentation system |
CN116139769A (en) * | 2022-11-03 | 2023-05-23 | 郑州嵩山硼业科技有限公司 | Special granulating method for pressureless sintering ceramic |
-
2018
- 2018-06-05 CN CN201810566839.XA patent/CN108839285A/en not_active Withdrawn
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112140493A (en) * | 2020-09-03 | 2020-12-29 | 南通顺驰橡胶制品有限公司 | Production process for preparing new butyl rubber inner tube by utilizing waste butyl rubber inner tube |
CN112140493B (en) * | 2020-09-03 | 2021-07-16 | 南通顺驰橡胶制品有限公司 | Production process for preparing new butyl rubber inner tube by utilizing waste butyl rubber inner tube |
CN113666532A (en) * | 2021-08-09 | 2021-11-19 | 滁州永强汽车制造有限公司 | Flocculation sedimentation system |
CN116139769A (en) * | 2022-11-03 | 2023-05-23 | 郑州嵩山硼业科技有限公司 | Special granulating method for pressureless sintering ceramic |
CN116139769B (en) * | 2022-11-03 | 2023-12-19 | 郑州嵩山硼业科技有限公司 | Special granulating method for pressureless sintering ceramic |
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Application publication date: 20181120 |