CN107030921A - A kind of production method of petrochemical industry occasion corrosion resistant anti-explosion cable sheath material - Google Patents

A kind of production method of petrochemical industry occasion corrosion resistant anti-explosion cable sheath material Download PDF

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Publication number
CN107030921A
CN107030921A CN201710200331.3A CN201710200331A CN107030921A CN 107030921 A CN107030921 A CN 107030921A CN 201710200331 A CN201710200331 A CN 201710200331A CN 107030921 A CN107030921 A CN 107030921A
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CN
China
Prior art keywords
production method
petrochemical industry
corrosion resistant
cable sheath
explosion
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
CN201710200331.3A
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Chinese (zh)
Inventor
陈赟
胡永斌
李忠林
翁志宝
吴华
胡元祥
查竞桃
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JIANGSU CHANGCHENG CABLE CO Ltd
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JIANGSU CHANGCHENG CABLE 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.)
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Application filed by JIANGSU CHANGCHENG CABLE CO Ltd filed Critical JIANGSU CHANGCHENG CABLE CO Ltd
Priority to CN201710200331.3A priority Critical patent/CN107030921A/en
Publication of CN107030921A publication Critical patent/CN107030921A/en
Pending legal-status Critical Current

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    • 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
    • B29B9/00Making granules
    • B29B9/02Making granules by dividing preformed material
    • B29B9/06Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/02Flame or fire retardant/resistant
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/04Antistatic
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/20Applications use in electrical or conductive gadgets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Insulated Conductors (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)

Abstract

A kind of production method of petrochemical industry occasion corrosion resistant anti-explosion cable sheath material, invention is related to the production technology of cable, dried after raw material is well mixed, it is subsequently placed in double-screw plastic extrusion machine and extrudes continuous material, successively by being extruded by as little as high five working regions of temperature, then cool down, then continuous material is cut into bulk material.The inventive method is simple, reasonable, petrochemical industry occasion corrosion resistant anti-explosion cable sheath is made under the erosion of oil fog in the bulk material being made after hot melt, it can be used 30 years, it is resistant to 150 160 DEG C of hot water and steam, fire resistance is strong, and modulus of elasticity reaches 2800/3300MPa at 120 DEG C, antistatic effect is good, and explosion-proof performance is good.

Description

A kind of production method of petrochemical industry occasion corrosion resistant anti-explosion cable sheath material
Technical field
The present invention relates to the production technical field of the production technology of cable, particularly cable sheath material.
Background technology
The raw materials for production of existing cable sheath are mainly polyolefin, epoxy resin, silane coupler and fire retardant, technique It is:After raw material is well mixed, it is placed in single-screw extruder, extrudes continuous material, the material of extrusion is directly by leading Draw and fall into pond cooling, material cutting granulates after cooling, packed after overall drying.
The defect of existing production technology is:The efficiency of extrusion plastic is low, and complex procedures, cooling effect is not good, is easily caused Plastic product particle deformation.
The content of the invention
The present invention seeks to propose that a kind of corrosion resistant that can overcome above prior art defect, that suitable oiling workshop is shared is anti- The production method of quick-fried cable sheath material.
The technical scheme is that:Dried after raw material is well mixed, be subsequently placed in double-screw plastic extrusion machine and extrude Continuous material, successively by being extruded by as little as high five working regions of temperature, is then cooled down, then continuous material cutting is granulated Material.
The inventive method is simple, reasonable, and feature is after raw material is well mixed, to be extruded again after drying, and And, successively by being extruded by as little as high five working regions of temperature, then cool down.The bulk material being made of the inventive method Petrochemical industry occasion corrosion resistant anti-explosion cable sheath is made after hot melt has advantages below:
1st, petrochemical industry occasion, under the erosion of oil fog, can be used 30 years.
2nd, 150-160 DEG C of hot water and steam are resistant to, GB/ can be passed through by GB/T10125-2012 salt spray test First method in T9274-2012(Infusion method)Acid resistance and alkaline resistance test, comprehensive corrosion resistance grade reaches B grades.
3rd, fire resistance is strong, can pass through A as defined in IEC60332 grades of fire retardancy test.
4th, modulus of elasticity reaches 2800/3300MPa at 120 DEG C, all better than other any hybrid resin materials.
5th, antistatic effect is good, and explosion-proof performance is good, in use, will not be rubbed because of with ground or other objects Wipe, produce electrostatic.
Further, raw material of the present invention is by polyolefin, polyether sulfone, aqueous polyurethane, epoxy resin, silane coupled Agent, toughener, antistatic additive, fire retardant and anti-wear agent composition.Petrochemical industry application requirements cable has the explosion-proof performance of corrosion resistant, Therefore corresponding performance must also be possessed by being directly wrapped in the sheath material of cable outer layer.
Accessible special excellent results:The addition of polyether sulfone and aqueous polyurethane, can make cable jacket material have one Fixed antiseptic property, while the toughener and anti-wear agent that add, more improve the toughness and anti-wear performance of sheath material, make electricity Cable reduces abrasion in dragging or work progress;The addition of antistatic additive so that sheath material will not in cable moving process Friction with other objects causes electrostatic, increases explosion-proof performance, while also having certain anti-electromagnetic interference performance;Fire retardant Add so that cable sheath material has certain flame retardant effect.
It is the polyolefin, polyether sulfone, aqueous polyurethane, epoxy resin, silane coupler, toughener, antistatic additive, fire-retardant Agent and anti-wear agent account for raw material and always feed intake 30~38%, 28~34%, 10~16%, 12~15%, 0.1~0.3%, the 0.2 of quality respectively ~0.5%, 0.4~0.8%, 1.0~2.0%, 1.2~1.6%.The design starting point of the proportioning of above raw material:Consider petrochemical industry The property of all-in-one cable, cable and cable sheath material must have certain property, such as corrosion resistant performance, explosion-proof Performance, fire resistance, interference free performance etc., therefore, either petrochemical industry all-in-one cable, or its cable sheath material Material, it is necessary to reach these performances.But found during research sheath material proportioning, corrosion resistant performance requires the anti-of material Corrosive power is strong, and explosion-proof performance requires that material has certain electric conductivity, but if material has certain electric conductivity Can, then the interference free performance of material will cannot be guaranteed, while the inherent electric current of material will cause its aging to accelerate, it is anticorrosive Performance is reduced, therefore, and the use characteristic of the sheath material of statolith oiling workshop all-in-one cable adds antistatic additive, wear-resisting Agent and aqueous polyurethane, it is ensured that while material explosion-proof performance, also increase the abrasion-proof corrosion-proof performance of material.
Accessible special excellent results:Make sheath material have excellent corrosion resistant performance, explosion-proof performance, fire resistance, Interference free performance, service life is long.
As little as high five working regions of the temperature are respectively 170~180 DEG C, 180~200 DEG C, 200~220 DEG C, 220 ~240 DEG C and 240~260 DEG C.Each temperature range more than using can make to mix with the temperature in the single each heating work region of control Condensation material enters after twin-screw, can slowly heat, and homogeneous heating, after the fluxing point temperature for reaching material, various materials Material can be good at being merged, and produce a kind of new material.
The cooling is to use water cooling and air-cooled combination.In material processing, the cooling side being typically used for Formula is water cooling or air-cooled.The mode of water cooling, cooling velocity is general, and section needs to dry again after cooling;Air-cooled mode, it is cold But speed is slow, and in cooling procedure, the plastics of extrusion molding may be deformed upon.By the way of water cooling and air-cooled combination, no But it need not be dried after accelerating cooling velocity, and cooling, can directly cut dress bag, occur during will not also cooling down again Deformation, particle is uneven when causing to cut.
Specific method is:Continuous material is passed through by draught line from cooling water, and continuous material is left after bosh, warp Cross hair-dryer progress air-cooled.Cooling effectiveness is high, and formed product rate is high.
Embodiment
1st, raw material is weighed:
Polyolefin 38kg, the kg of polyether sulfone 34, the kg of aqueous polyurethane 11, the kg of epoxy resin 12, silane coupler are weighed respectively 0.3 kg, the kg of toughener 0.5, the kg of antistatic additive 0.4~0.8, the kg of fire retardant 1.0~2.0, the kg of anti-wear agent 1.2~1.6, The kg of total amount 100.
2nd, production technology:
All raw materials are all uniformly mixed and dried, are then placed in double-screw plastic extrusion machine, by 5 workspaces of extruding machine The temperature in domain is set as 170~180 DEG C, 180~200 DEG C, 200~220 DEG C, 220~240 DEG C, 240~260 DEG C, treats that plastics are squeezed Go out after continuous material, cooled down by water cooling and air-cooled combination, be put into afterwards in sizing cutting machine and cut and granulate Material.
Specific water cooling and air-cooled combination are:The continuous material extruded from extruding machine directly passes through a draught line Pass through, left after bosh from cooling water, air-cooled cooling is carried out through excessive power hair-dryer, while by the residual on its surface Cooling water is removed.
3rd, apply:
Above bulk material is directly coated in cable outer layer as sheath after 250 DEG C of hot melt, cable is obtained after cooling.
Cable is tested, proved after tested:
1st, petrochemical industry occasion, under the erosion of oil fog, can be used 30 years.
2nd, 150-160 DEG C of hot water and steam are resistant to, GB/ can be passed through by GB/T10125-2012 salt spray test First method in T9274-2012(Infusion method)Acid resistance and alkaline resistance test, comprehensive corrosion resistance grade reaches B grades.
Sample size is long 200mm, wide 80mm strip.
In salt spray test, sample surfaces are without obvious corrosion phenomenon, and the mass loss amount of sample is less than 35 ± 2g/ of standard m2, result of the test is 28 g/m2, mass parameter is 670, reaches B grades of requirements;
In acid resisting test, sample surfaces are without obvious corrosion phenomenon, and the mass loss amount of sample is less than 30 ± 15g/ of standard m2, result of the test is 22 g/m2, mass parameter is 595, reaches B grades of requirements;
In alkaline resistance test, sample surfaces are without obvious corrosion phenomenon, and the mass loss amount of sample is less than 30 ± 15g/ of standard m2, result of the test is 18 g/m2, mass parameter is 784, reaches C grades of requirements;
Comprehensive corrosion resistance grade reaches B grades(Class requirement is with reference to the rotproofness grade in GB/T23639-2009 standards).
3rd, fire resistance is strong, can pass through A as defined in IEC60332 grades of fire retardancy test.
Experimental condition:For fiery time 40min.
The length carbonized on sample and the upward distance in nozzle base, standard is maximum 2.5m, and result of the test is 0.9m, is closed Lattice.
Stop for the flaming combustion time after fire on sample, standard is maximum 1h, and result of the test is 0.1h, qualified.
4th, modulus of elasticity reaches 2800/3300MPa at 120 DEG C, all better than other any hybrid resin materials.
5th, antistatic effect is good, and explosion-proof performance is good, in use, will not be rubbed because of with ground or other objects Wipe, produce electrostatic.

Claims (6)

1. a kind of production method of petrochemical industry occasion corrosion resistant anti-explosion cable sheath material, it is characterised in that raw material is mixed equal Dried after even, be subsequently placed in double-screw plastic extrusion machine and extrude continuous material, successively by by as little as high five work of temperature Region is extruded, and is then cooled down, then continuous material is cut into bulk material.
2. production method according to claim 1, it is characterised in that:The raw material is by polyolefin, polyether sulfone, aqueous poly- ammonia Ester, epoxy resin, silane coupler, toughener, antistatic additive, fire retardant and anti-wear agent composition.
3. production method according to claim 2, it is characterised in that:The polyolefin, polyether sulfone, aqueous polyurethane, ring Oxygen tree fat, silane coupler, toughener, antistatic additive, fire retardant and anti-wear agent account for respectively raw material always feed intake quality 30~ 38%th, 28~34%, 10~16%, 12~15%, 0.1~0.3%, 0.2~0.5%, 0.4~0.8%, 1.0~2.0%, 1.2~ 1.6%。
4. the production method according to claim 1 or 2 or 3, it is characterised in that:As little as high five working regions of the temperature Respectively 170~180 DEG C, 180~200 DEG C, 200~220 DEG C, 220~240 DEG C and 240~260 DEG C.
5. production method according to claim 1, it is characterised in that:The cooling is to use water cooling and air-cooled combination side Formula.
6. production method according to claim 5, it is characterised in that:Continuous material is worn by draught line from cooling water Cross, continuous material is left after bosh, carried out by hair-dryer air-cooled.
CN201710200331.3A 2017-03-30 2017-03-30 A kind of production method of petrochemical industry occasion corrosion resistant anti-explosion cable sheath material Pending CN107030921A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108943652A (en) * 2018-07-18 2018-12-07 徐州工业职业技术学院 A kind of rubber semi-products extrusion cooling process method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005153397A (en) * 2003-11-27 2005-06-16 Hitachi Cable Ltd Method for producing electric wire cable
CN103709486A (en) * 2013-12-31 2014-04-09 广东三凌塑料管材有限公司 Polyethylene cable protective casing pipe
CN204278487U (en) * 2014-11-05 2015-04-22 重庆鸿岱科技有限公司 Plastic granulator device for drying and cooling assembly
CN205247948U (en) * 2015-11-28 2016-05-18 苏州安骐尔电缆科技有限公司 Control cable

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005153397A (en) * 2003-11-27 2005-06-16 Hitachi Cable Ltd Method for producing electric wire cable
CN103709486A (en) * 2013-12-31 2014-04-09 广东三凌塑料管材有限公司 Polyethylene cable protective casing pipe
CN204278487U (en) * 2014-11-05 2015-04-22 重庆鸿岱科技有限公司 Plastic granulator device for drying and cooling assembly
CN205247948U (en) * 2015-11-28 2016-05-18 苏州安骐尔电缆科技有限公司 Control cable

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108943652A (en) * 2018-07-18 2018-12-07 徐州工业职业技术学院 A kind of rubber semi-products extrusion cooling process method

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