The content of the invention
The purpose of the utility model is to overcome defect existing in the prior art, there is provided it is automatic that one kind is suitable for production line
The heat shrink films of fast package.
The technical problem that the utility model solves is:1. heat sealability-the low-temperature heat-sealing and heat seal strength of film will height;
2. film walks machine performance-preferable film flatness, flexibility;3. the shrinkage of film-higher percent thermal shrinkage.
Original technology:1) blown film 2) printing-bag making 3) hand-filling 4) vacuum-pumping and sealing 5) thermal contraction-packed products.And
The utility model:1) blown film 2) printing-cutting 3) on machine pack automatically-cuts-vacuum-pumping and sealing-thermal contraction-packed products, greatly
It is big to improve packaging efficiency, operating process and step are reduced, reduces the pollution risk of product.There is the utility model contraction bag to be gathered around
Some excellent properties high-barriers, high intensity, heat sealability is good, at the same have it is excellent walk machine performance, suitable for full-automatic online
Packaging.
The first aspect of the utility model, there is provided a kind of heat shrink films suitable for the automatic fast package of production line, including
Positioned at the top layer of outer surface, positioned at the hot sealing layer of inner surface, and the barrier layer being arranged between top layer and hot sealing layer;The resistance
Interlayer includes one layer of ethylene-vinyl alcohol copolymer (EVOH) and obstructs intermediate layer, and EVOH barriers intermediate layer at least side is set
There is one layer of barrier layer protective layer, the barrier layer protective layer is polyamide (PA) layer;The top layer is PA layers or polyester
(PET) layer;The hot sealing layer is POP layers or metallocene linear low density polyethylene (mLLDPE) layer, ultra-low density polyethylene
(ULDPE) one kind in layer, Surlyn resin beds, or the blended layer of POP and mLLDPE;The top layer and barrier layer, barrier
Connected respectively by adhering resin (abbreviation Tie) between layer and hot sealing layer.
The polyester (PET), the polymer general name as obtained by polyalcohol and polyacid polycondensation, refers mainly to poly- terephthaldehyde
Sour second diester.Equipolymers, EASTMAN, the Dufor trades mark C series, GN series, FX series etc. may be selected.
The Surlyn resins are that du pont company of Du Pont is polymerized using unique production technology, are by high pressure
The ethylene-methacrylic acid copolymer of radical polymerization is through partly or entirely neutralizing and a kind of manufactured copolymer.
The POP is vinyl polymer graft polyether polyol, is commonly called as " polymer polyatomic alcohol " (Polyether
Polyol), abbreviation polyethers (POP), is the thermoplastic elastic that in-situ polymerization is realized using the ethene and octene of metallocene catalyst
Body.SABIC, Exxonmobil, DOW trades mark COHERE8380, COHERE8185,9061,9071,9182 may be selected,
KC8852G, VP8770G1,1881G, 1850G etc..
Metallocene linear low density polyethylene (the metallocene linear low density
Polyethylene, abbreviation mLLDPE) with metallocene compound catalyst is made, there is narrow ditribution molecule through what coordination polymerization obtained
The ethene of amount and the linear copolymers of thing-alkene.PRIME, Exxonmobil, the DOW trade mark 1018MF, 2018KB may be selected,
1012HJ, SP 1520 etc..
Preferably, structure sheaf is equipped between the top layer and barrier layer, the structure sheaf is selected from polyethylene (PE)
Layer, ethylene-vinyl acetate copolymer (EVA) layer, POP layers, one or both of PP layers of blended layer, the structure sheaf with
Connected respectively by adhering resin between top layer, barrier layer.It is furthermore preferred that the PE is compared with low-density (≤0.91g/cm3)
PE.Exxonmobil, DuPont, DOW trades mark 701,705,3165,3129,1881,1850 etc. may be selected.
Preferably, secondary internal layer is additionally provided between the hot sealing layer and barrier layer, the secondary internal layer is selected from polyethylene
(PE) layer, ethylene-vinyl acetate copolymer (EVA) layer, one or both of POP layers of blended layer, the secondary internal layer with
Connected between barrier layer by adhering resin.
Preferably, formed by PA6, copolymerization PA and unformed PA blendings for described top layer PA layers, unformed PA in resin
Mass percent is 10~30% (more preferably 20%), and the mass percent for being copolymerized PA (is more preferably for 10~60%
10%).
Preferably, the resin of the PA layers of the barrier layer protective layer is formed by PA6, copolymerization PA and unformed PA blendings,
The mass percent of unformed PA is not more than 40% in PA layers of resin.
Preferably, the PA, copolymerization PA, the relative viscosity 3.5-4.17 of unformed PA, density 1.12-1.19g/cm3。
Preferably, the hot sealing layer is the blended layer of POP and mLLDPE, and the content of POP is 30- wherein in hot sealing layer
90% (more preferably 50%).
Preferably, the film layer number of the heat shrink films suitable for the automatic fast package of production line is 4~11 layers.
Preferably, the gross thickness of the heat shrink films suitable for the automatic fast package of production line is (excellent for 40~100um
Select 75um).Wherein top layer accounts for the 5-15% of gross thickness, and barrier layer accounts for the 4-10% of gross thickness, and hot sealing layer accounts for the 18- of gross thickness
35%, structure sheaf accounts for the 30-50% of gross thickness.
Preferably, the heat shrink films:Longitudinal direction/lateral shrinkage 20-45 (90 DEG C), elongation 80-180, surface
36-40 dynes of power, heat play 80-90 DEG C of temperature of envelope, 90-220 DEG C of fusing point.
Preferably, opening agent is further included in the hot sealing layer, extexine further includes slipping agent.
In a preferred embodiment of the utility model, the heat shrink films include top layer successively from outside to inside
(PA), structure sheaf (PE), barrier layer (PA/EVOH/PA, including EVOH barrier intermediate layers and the barrier layer protective layers of both sides are PA
Layer), hot sealing layer (POP+mLLDPE).Pass through adhering resin respectively between the top layer, structure sheaf, barrier layer and hot sealing layer
(Tie) connect.
Specifically membrane structure is:PA/Tie/PE/Tie/PA/EVOH/PA/Tie/POP+mLLDPE;
Wherein top layer and PA two layers middle are formed using PA6, copolymerization PA and unformed PA blendings, in PA layers of resin
The mass percent for being copolymerized PA is 10%, and the content of hot sealing layer POP is 90%, overall film thickness 75um.
In other preferred embodiments of the utility model, the heat shrink films specific membrane structure choosing from outside to inside
From:
PA/Tie/PA/EVOH/PA/Tie/POP;
PA/Tie/PA/EVOH/PA/Tie/POP+mLLDPE;
PA/Tie/PE/Tie/EVOH/PA/Tie/mLLDPE;
PA/Tie/EVA/Tie/EVOH/PA/Tie/mLLDPE;
PA/Tie/EVOH/PA/Tie/POP;
PA/Tie/EVOH/PA/Tie/mLLDPE;
PA/Tie/EVOH/PA/Tie/POP+mLLDPE;
PA/Tie/EVA/Tie/PA/EVOH/PA/Tie/POP;
PA/Tie/EVA/Tie/PA/EVOH/PA/Tie/mLLDPE;
PA/Tie/EVA/Tie/PA/EVOH/PA/Tie/POP+mLLDPE;
PET/Tie/PE/Tie/PA/EVOH/PA/Tie/PE;
PET/Tie/PE/Tie/PA/EVOH/PA/Tie/POP;
PET/Tie/PE/Tie/PA/EVOH/PA/Tie/mLLDPE;
PET/Tie/PE/Tie/PA/EVOH/PA/Tie/POP+mLLDPE;
PET/Tie/PP/Tie/PA/EVOH/PA/Tie/PE;
PET/Tie/PP/Tie/PA/EVOH/PA/Tie/POP;
PET/Tie/PP/Tie/PA/EVOH/PA/Tie/mLLDPE;
PET/Tie/PP/Tie/PA/EVOH/PA/Tie/POP+mLLDPE;
PET/Tie/EVA/Tie/PA/EVOH/PA/Tie/PE;
PET/Tie/EVA/Tie/PA/EVOH/PA/Tie/POP;
PET/Tie/EVA/Tie/PA/EVOH/PA/Tie/mLLDPE;
PET/Tie/EVA/Tie/PA/EVOH/PA/Tie/POP+mLLDPE。
In a preferred embodiment of the utility model, the specific membrane structure of the heat shrink films is:
PA/Tie/EVA/Tie/PA/EVOH/PA/Tie/POP+mLLDPE。
A kind of third aspect of the utility model, there is provided heat receipts as described above suitable for the automatic fast package of production line
The production technology of contracting film, comprises the following steps:
Production technology, including the shaping of extrusion plasticizing, Multi-layer coextruding die head, cooling water quenching, the preheating of the first membrane tube, secondary blow
Swollen, traction, thermal finalization, traction, winding, in Multi-layer coextruding die head forming step to formed the PA resins of barrier layer protective layer plus
Hot temperature is 255~265 DEG C, and the temperature of cooling water is 5~15 DEG C in cooling water quenching fixating shape step.The POP and PE of hot sealing layer
Heating-up temperature be 220~230 DEG C.
Preferably, following steps are specifically included:
S1:Raw material is placed in co-extrusion in extruder and obtains membrane tube, to membrane tube cooling treatment;
S2:Membrane tube after cooling is heated to preheating temperature, membrane tube is stretched, is then carried out using compressed air secondary
Inflation;
S3:By packaging film feeding obtained by secondary inflation to shaping mechanism, it is again heated to setting temperature and shaping film is handled,
Obtain multi-layer co-extruded shrink film finished product.
Wherein, S1 coextruded films are from top to bottom extruded using water cooling, are realized that film is sudden cold, the generation of crystallization are controlled, with profit
In the orientation of molecule segment, the mist degree of film can be reduced.Preferably, the water-cooled process water temperature in S1 is 5~15 DEG C, flow velocity 20
~35L/min.
Preferably, preheating temperature is 30~80 DEG C in S2;The blow-up ratio of secondary inflation is 1.5~4, draw ratio for 2.5~
3.0.The blow-up ratio and draw ratio and the crystallinity of coextruded film in S1 of secondary inflation match.Blow-up ratio and draw ratio too great Rong
It is unstable to easily cause film bubble, and fold easily occurs in film;The shrinking percentage of too small then finished product is less than 30%, does not reach finished product packing
Requirement.
Preferably, setting temperature is 30~70 DEG C in S3.The styling of three bubbles can effectively suppress ordinary convergence film
Free shrink in storing process (at a temperature of storage environment, the natural disorientation of strand).
It is furthermore preferred that the water-cooled process water temperature in S1 is 10 DEG C, flow velocity is 20~30L/min.
Preheating temperature is 75 DEG C in S2;The blow-up ratio of secondary inflation is 3.0, draw ratio 3.0.
Setting temperature is 60 DEG C in S3.
Compared with prior art, the utility model advantages and beneficial effects are:
1st, the selection of heat-sealable material:Ability and heat-sealing Hot Tack strength are sealed to improve the antipollution of material, is made in hot sealing layer
With materials such as POP, ULDPE, SURLYN;Hot sealing layer employs density in 0.9g/cm3The PE hot sealing layers of left and right, or sarin heat-sealing
Layer.With excellent low temperature heat seal and efficient antipollution heat sealability.Play envelope temperature reduces 10-20 DEG C than conventional material.
Except low envelope temperature, it is also necessary to improve the heat seal strength rate of climb, i.e., in same temperature range, heat-sealing is strong
Degree increase is more.The material of usual low melting point have it is relatively low play envelope temperature, but its heat seal strength is accordingly weaker, it is quick from
During dynamic packaging, since material heated time is shorter, moment heat seal strength can not enough cause heat-sealing problem, therefore reduce
While having sealed envelope temperature, it is the big main points that this automatic packaging line application need to solve to improve heat seal strength.This practicality is new
Type does auxiliary heat-sealing by hot sealing layer and secondary internal layer, to reach the coordination of low envelope temperature and high heat-sealing strength.
2nd, film flatness:The pliability of film is controlled by the selection of structural material, using compared with low-density≤
0.91g/cm3PE, or the relatively soft material such as EVA is used in structure sheaf, makes it have preferable film flatness, flexibility.
3. the shrinkage of film:On the one hand controlled, on the other hand controlled by material, especially by process conditions
It is the shrinking percentage that PA layer materials can limit film, the slower PA materials of selective freezing, increase the ratio of copolymer nylon, addition is without fixed
Type nylon etc. improves the shrinking percentage of film.
The new heat shrink films of the utility model have the excellent properties high-barrier that contraction bag is possessed, high intensity, heat-sealing
Performance is good, at the same have it is excellent walk machine performance, suitable for automatically the bag of contraction bag will be changed in wire wrapping, the utility model
Dress mode and packaging efficiency.