CN111993616A - Efficient BR and SBR rubber dissolving equipment - Google Patents

Efficient BR and SBR rubber dissolving equipment Download PDF

Info

Publication number
CN111993616A
CN111993616A CN202010795811.0A CN202010795811A CN111993616A CN 111993616 A CN111993616 A CN 111993616A CN 202010795811 A CN202010795811 A CN 202010795811A CN 111993616 A CN111993616 A CN 111993616A
Authority
CN
China
Prior art keywords
rubber
dissolving
tank
styrene
pipe
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
Application number
CN202010795811.0A
Other languages
Chinese (zh)
Inventor
陶春风
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangxi Changke New Material Co ltd
Original Assignee
Guangxi Changke New Material Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangxi Changke New Material Co ltd filed Critical Guangxi Changke New Material Co ltd
Priority to CN202010795811.0A priority Critical patent/CN111993616A/en
Publication of CN111993616A publication Critical patent/CN111993616A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/06Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
    • B29B7/10Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
    • B29B7/12Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with single shaft
    • B29B7/16Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with single shaft with paddles or arms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/06Spray cleaning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B13/00Conditioning or physical treatment of the material to be shaped
    • B29B13/10Conditioning or physical treatment of the material to be shaped by grinding, e.g. by triturating; by sieving; by filtering
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/22Component parts, details or accessories; Auxiliary operations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/22Component parts, details or accessories; Auxiliary operations
    • B29B7/24Component parts, details or accessories; Auxiliary operations for feeding

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

The invention relates to a dissolving device for high-efficiency BR and SBR rubber, which comprises a rubber dissolving tank and a rubber feeding tank opening arranged at the top of the rubber dissolving tank, wherein a rubber crusher is hermetically arranged at the top of the rubber feeding tank opening, a styrene supply pipe is arranged on the outer side of the rubber dissolving tank, and a styrene spraying mechanism connected with a styrene supply branch pipe is arranged at the rubber feeding tank opening; a material stirring mechanism is arranged in the rubber dissolving tank, and the bottom of the rubber dissolving tank is connected with a circulating grinding mechanism; the equipment adopts an efficient stirrer to realize the sufficient and uniform mixing of rubber and styrene monomers and eliminate a mixing dead zone in the tank; a styrene spraying mechanism is arranged at the mouth of the rubber feeding tank, so that dust removal is facilitated and the rubber particles are prevented from being hung on the wall; the rubber feeding tank opening is also connected with a nitrogen supply pipe, and the design of inlet nitrogen sealing and micro negative pressure of the rubber dissolving tank is adopted to prevent air from entering and peculiar smell from leaking; and a circulating grinding mechanism is arranged, so that the dissolving process is accelerated, and the dissolving efficiency and quality are ensured.

Description

Efficient BR and SBR rubber dissolving equipment
Technical Field
The invention relates to the field of chemical equipment, in particular to efficient BR and SBR rubber dissolving equipment.
Background
In HIPS and body ABS resin production field, dissolve quantitative BR \ SBR rubber in styrene monomer, it is an indispensable step in HIPS and body ABS resin production process to formulate styrene rubber solution, present rubber dissolving tank exists the stirring inhomogeneous, the rubber fritter is gathered into the heap in the jar, rubber does not realize totally closed feeding, there is styrene gas in the rubber feed inlet to escape from the below, or the phenomenon of entering dissolving tank under the air, dangerous and on-the-spot peculiar smell is very big, seriously influence the safe and stable operation of device, this patent carries out rubber dissolving equipment structural improvement based on above technical problem.
Disclosure of Invention
The invention aims to solve the defects in the prior art and provide efficient BR and SBR rubber dissolving equipment.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
a dissolving device for high-efficiency BR and SBR rubber comprises a rubber dissolving tank, a rubber feeding tank opening arranged at the top of the rubber dissolving tank, a rubber crusher arranged at the top of the rubber feeding tank opening in a sealing manner, a styrene supply pipe arranged at the outer side of the rubber dissolving tank, the styrene supply pipe connected with the rubber feeding tank opening through a first styrene supply branch pipe, the styrene supply pipe connected with a body unit of the rubber dissolving tank through a second styrene supply branch pipe, and a styrene spraying mechanism connected with the first styrene supply branch pipe arranged at the rubber feeding tank opening;
the rubber dissolving tank is internally provided with a material stirring mechanism, and the bottom of the rubber dissolving tank is connected with a circulating grinding mechanism.
Further, the styrene spraying mechanism comprises an annular pipe connected with the first styrene supply branch pipe and a spraying head arranged on the annular pipe, and the port of the spraying head faces the rubber dissolving tank.
Further, the material stirring mechanism comprises a stirring shaft arranged in the rubber dissolving tank, and stirring blades arranged on the stirring shaft, wherein a stirring motor connected with the stirring shaft is arranged at the top of the rubber dissolving tank.
Further, the circulating grinding mechanism comprises a circulating delivery pipe connected with the bottom of the rubber dissolving tank, a grinding circulating pump connected with the circulating delivery pipe, and a plurality of circulating inlet pipes connected with the output end of the grinding circulating pump, wherein the circulating inlet pipes are connected with the top and the bottom of the rubber dissolving tank.
Furthermore, a throttle valve is installed on the circulating delivery pipe, the output end of the grinding circulating pump is also connected with a liquid outlet pipe, a valve is installed on the liquid outlet pipe, and the liquid outlet pipe is connected with the polymerization unit.
Furthermore, the rubber feeding tank opening is also connected with a nitrogen supply pipe, and the top of the rubber dissolving tank is connected with a tail gas delivery pipe.
Further, one side of the rubber crushing machine is provided with a rubber block conveying belt.
The invention has the beneficial effects that: 1. an efficient stirrer is selected to realize the full and uniform mixing of rubber and styrene monomers and eliminate a mixing dead zone in the tank; 2. a styrene spraying mechanism is arranged at the mouth of the rubber feeding tank, so that dust removal is facilitated and the rubber particles are prevented from being hung on the wall; 3. the rubber feeding tank opening is also connected with a nitrogen supply pipe, and the design of inlet nitrogen sealing and micro negative pressure of the rubber dissolving tank is adopted to prevent air from entering and peculiar smell from leaking; 4. and a circulating grinding mechanism is arranged, so that the dissolving process is accelerated, and the dissolving efficiency and quality are ensured.
Drawings
FIG. 1 is a schematic structural diagram of the present invention.
Detailed Description
As shown in figure 1, the dissolving device for high-efficiency BR and SBR rubber comprises a rubber dissolving tank 1, a rubber feeding tank opening 2 arranged at the top of the rubber dissolving tank 1, a rubber crusher 3 arranged at the top of the rubber feeding tank opening 2 in a sealing way, a styrene supply pipe 4 arranged at the outer side of the rubber dissolving tank 1, the styrene supply pipe 4 connected with the rubber feeding tank opening 2 through a first styrene supply branch pipe 5, the styrene supply pipe 4 connected with a body unit of the rubber dissolving tank 1 through a second styrene supply branch pipe 6, and a styrene spraying mechanism connected with the first styrene supply branch pipe 5 arranged at the rubber feeding tank opening 2; a material stirring mechanism is arranged in the rubber dissolving tank 1, and the bottom of the rubber dissolving tank is connected with a circulating grinding mechanism.
Further, the styrene spraying mechanism includes a ring pipe 7 connected to the first styrene supply branch pipe 5 and a spray header 8 mounted on the ring pipe 7, and a port of the spray header 8 faces the rubber dissolving tank 1.
The material stirring mechanism comprises a stirring shaft 9 arranged in the rubber dissolving tank 1 and a stirring paddle blade 10 arranged on the stirring shaft 9, and the top of the rubber dissolving tank 1 is provided with a stirring motor 11 connected with the stirring shaft 9. The material stirring mechanism achieves the purpose of fast reaction and dissolution of rubber particles and styrene in the rubber dissolving tank 1.
Further, the circulating grinding mechanism comprises a circulating delivery pipe 12 connected with the bottom of the rubber dissolving tank 1, a grinding circulating pump 13 connected with the circulating delivery pipe 12, and a plurality of circulating inlet pipes 14 connected with the output end of the grinding circulating pump 13, wherein the circulating inlet pipes 14 are connected with the top and the bottom of the rubber dissolving tank 1. The circulating delivery pipe 12 is provided with a throttle valve 15, the output end of the grinding circulating pump 13 is also connected with a liquid outlet pipe 16, the liquid outlet pipe 16 is provided with a valve 17, and the liquid outlet pipe 16 is connected with the polymerization unit.
Further, the nitrogen gas supply pipe 18 is also connected to the rubber feed tank port 2, and nitrogen gas introduced by the nitrogen gas supply pipe 18 at a high speed plays a role in nitrogen sealing to the rubber feed tank port 2, and plays a role in micro negative pressure of a rubber dissolving tank, so that air entering and peculiar smell leakage are prevented.
The top of the rubber dissolving tank 1 is connected with a tail gas delivery pipe 19, and one side of the rubber crushing machine 3 is provided with a rubber block conveying belt 20.
When the equipment is processed, a rubber block conveyer belt 20 conveys a rubber block 21 to a rubber crusher 3 to be cut and crushed to form rubber particles, the rubber particles fall into a rubber dissolving tank 1, meanwhile, a styrene supply pipe 4 guides styrene into the rubber dissolving tank 1 to dissolve the rubber particles to form a styrene rubber solution, meanwhile, a stirring motor 11 drives a stirring paddle blade 10 to rotate to stir the solution, so that the dissolving speed is accelerated, in the processing process, the styrene sprayed by a spray head 8 at a rubber feeding tank port 2 is in contact with dust, so that the effects of dedusting and preventing the rubber particles from being hung on the wall are achieved, in addition, a nitrogen supply pipe 18 at the rubber feeding tank port 2 is used for introducing nitrogen at a high speed, and an inlet nitrogen seal and a micro negative pressure design of the rubber dissolving tank are adopted, so that air cross-in and peculiar smell are prevented from leaking;
in addition, during the reaction processing, the grinding circulating pump 13 is used for leading out the solution in the rubber dissolving tank 1 at regular time for circulating grinding, so that the auxiliary processing effect is achieved, the dissolving process is accelerated, and the dissolving efficiency and quality are ensured.
In conclusion, the equipment adopts the efficient stirrer to realize the full and uniform mixing of the rubber and the styrene monomer and eliminate the mixing dead zone in the tank; a styrene spraying mechanism is arranged at the mouth of the rubber feeding tank, so that dust removal is facilitated and the rubber particles are prevented from being hung on the wall; the rubber feeding tank opening is also connected with a nitrogen supply pipe, and the design of inlet nitrogen sealing and micro negative pressure of the rubber dissolving tank is adopted to prevent air from entering and peculiar smell from leaking; and a circulating grinding mechanism is arranged, so that the dissolving process is accelerated, and the dissolving efficiency and quality are ensured.
The foregoing shows and describes the general principles, essential features, and advantages of the invention. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are merely illustrative of the principles of the invention, but that various changes and modifications may be made without departing from the spirit and scope of the invention, which fall within the scope of the invention as claimed. The scope of the invention is defined by the appended claims and equivalents thereof.

Claims (7)

1. A dissolving device for high-efficiency BR and SBR rubber comprises a rubber dissolving tank and a rubber feeding tank opening arranged at the top of the rubber dissolving tank, and is characterized in that a rubber crusher is hermetically arranged at the top of the rubber feeding tank opening, a styrene supply pipe is arranged on the outer side of the rubber dissolving tank, the styrene supply pipe is connected with the rubber feeding tank opening through a first styrene supply branch pipe, the styrene supply pipe is connected with a body unit of the rubber dissolving tank through a second styrene supply branch pipe, and a styrene spraying mechanism connected with the first styrene supply branch pipe is arranged at the rubber feeding tank opening;
the rubber dissolving tank is internally provided with a material stirring mechanism, and the bottom of the rubber dissolving tank is connected with a circulating grinding mechanism.
2. The dissolving apparatus for BR and SBR rubber according to claim 1, wherein said styrene spraying means comprises a ring pipe connected to the first styrene supply branch pipe and a spray header installed on the ring pipe, and a port of the spray header faces the rubber dissolving tank.
3. The dissolving equipment for high-efficiency BR and SBR rubber according to claim 1 or 2, wherein the material stirring mechanism comprises a stirring shaft arranged in the rubber dissolving tank, and a stirring blade arranged on the stirring shaft, and the top of the rubber dissolving tank is provided with a stirring motor connected with the stirring shaft.
4. The dissolving apparatus for BR and SBR rubber according to claim 3, wherein the circulating grinding mechanism comprises a plurality of circulating lead-in pipes connected to the bottom of the rubber dissolving tank, a grinding circulation pump connected to the circulating lead-out pipe, and a circulating lead-in pipe connected to the output end of the grinding circulation pump, the circulating lead-in pipes being connected to the top and bottom of the rubber dissolving tank.
5. The efficient BR and SBR rubber dissolving apparatus of claim 4, wherein said recycle outlet pipe is provided with a throttle valve, the output end of said grinding recycle pump is further connected to a drain pipe, the drain pipe is provided with a valve, and the drain pipe is connected to said polymerization unit.
6. The dissolving apparatus for BR and SBR rubber according to claim 4, wherein a nitrogen supply pipe is further connected to the rubber feed tank port, and an exhaust gas delivery pipe is connected to the top of the rubber dissolving tank.
7. The dissolving apparatus for BR and SBR rubber according to claim 4, wherein said rubber crusher is provided with a rubber block conveyer at one side thereof.
CN202010795811.0A 2020-08-10 2020-08-10 Efficient BR and SBR rubber dissolving equipment Pending CN111993616A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010795811.0A CN111993616A (en) 2020-08-10 2020-08-10 Efficient BR and SBR rubber dissolving equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010795811.0A CN111993616A (en) 2020-08-10 2020-08-10 Efficient BR and SBR rubber dissolving equipment

Publications (1)

Publication Number Publication Date
CN111993616A true CN111993616A (en) 2020-11-27

Family

ID=73463356

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010795811.0A Pending CN111993616A (en) 2020-08-10 2020-08-10 Efficient BR and SBR rubber dissolving equipment

Country Status (1)

Country Link
CN (1) CN111993616A (en)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1201797A (en) * 1997-04-08 1998-12-16 东洋工程公司 Method of continuously dissolving rubber
CN102344394A (en) * 2011-07-26 2012-02-08 河北克尔化工有限公司 Preparation method of nitroguanidine and its derivatives N-methylnitroguanidine and oxadiazine
DK2218565T3 (en) * 2007-02-15 2012-09-17 Erema Method and apparatus for processing a material
CN103476561A (en) * 2011-03-31 2013-12-25 三菱化学株式会社 Method for manufacturing polycarbonate resin, polycarbonate resin, and methods for manufacturing polycarbonate-resin film and polycarbonate-resin pellets
CN205323748U (en) * 2015-12-21 2016-06-22 长乐恒申合纤科技有限公司 Reaction unit is retrieved to prepolymer
CN206253023U (en) * 2016-11-30 2017-06-16 山东恒联新材料股份有限公司 A kind of cellulosics high viscosity viscose glue dissolver
EP3181591A1 (en) * 2012-06-18 2017-06-21 Bridgestone Corporation Methods for increasing the extractable rubber content of non-hevea plant matter
CN208975806U (en) * 2018-09-27 2019-06-14 青岛科润生物科技有限公司 A kind of stirring apparatus for reaction kettle with elevating hopper
CN110545929A (en) * 2017-02-24 2019-12-06 卡博陶粒有限公司 binder material for producing ceramic particles

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1201797A (en) * 1997-04-08 1998-12-16 东洋工程公司 Method of continuously dissolving rubber
DK2218565T3 (en) * 2007-02-15 2012-09-17 Erema Method and apparatus for processing a material
CN103476561A (en) * 2011-03-31 2013-12-25 三菱化学株式会社 Method for manufacturing polycarbonate resin, polycarbonate resin, and methods for manufacturing polycarbonate-resin film and polycarbonate-resin pellets
CN102344394A (en) * 2011-07-26 2012-02-08 河北克尔化工有限公司 Preparation method of nitroguanidine and its derivatives N-methylnitroguanidine and oxadiazine
EP3181591A1 (en) * 2012-06-18 2017-06-21 Bridgestone Corporation Methods for increasing the extractable rubber content of non-hevea plant matter
CN205323748U (en) * 2015-12-21 2016-06-22 长乐恒申合纤科技有限公司 Reaction unit is retrieved to prepolymer
CN206253023U (en) * 2016-11-30 2017-06-16 山东恒联新材料股份有限公司 A kind of cellulosics high viscosity viscose glue dissolver
CN110545929A (en) * 2017-02-24 2019-12-06 卡博陶粒有限公司 binder material for producing ceramic particles
CN208975806U (en) * 2018-09-27 2019-06-14 青岛科润生物科技有限公司 A kind of stirring apparatus for reaction kettle with elevating hopper

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李登新: "《固体废物处理与处置工程素质综合训练》", 31 August 2019, 中国环境出版社 *

Similar Documents

Publication Publication Date Title
CN111389246A (en) Shear mixing part and vacuum mixer using same
CN111993616A (en) Efficient BR and SBR rubber dissolving equipment
CN219356223U (en) Device for preparing aliphatic secondary alcohol ethoxylate
CN111498886A (en) By using pure CO2Device and method for treating calcium-based alkaline residues
CN204208501U (en) The anti-blocking solid-liquid mixer of a kind of high efficiency
CN203108450U (en) Liquid material stirring device
CN207418731U (en) A kind of dry-process anaerobic fermentation device
CN212559488U (en) By using pure CO2Device for treating calcium-based alkaline residue
CN209093296U (en) A kind of efficient wet mixer-granulator
CN210336504U (en) Resin dosing unit
CN208627233U (en) A kind of efficient wet mixer-granulator
CN206885851U (en) Funnel type storage tank
CN207187646U (en) A kind of high pressure homogenizer
CN117046361B (en) Device for wet feeding of powder materials and water treatment method thereof
CN103585906B (en) Terephthalic acid (TPA) powder reclaiming device and recovery method
CN111495253A (en) Dust removal method and device in dry powder dissolving and preparing process
CN212236865U (en) Vacuum feeding system of high-speed shearing powder mixer
CN217164021U (en) Powder-liquid mixing equipment
CN213032478U (en) Solution polymerization reaction device for polymer tackifier
CN209997624U (en) vacuum nitrogen adding device for reaction kettle
CN219399623U (en) Multistage styrene exhaust gas purification processing apparatus
CN209791448U (en) Device for batch production
CN219279544U (en) A treatment facility for waste water after phenolic resin production
CN209828989U (en) Demulsifier processing system
CN215250903U (en) Efficient spraying type enzymolysis equipment for production of cod collagen VC peptide

Legal Events

Date Code Title Description
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

Application publication date: 20201127

RJ01 Rejection of invention patent application after publication