Embodiment
Below in conjunction with accompanying drawing, the present invention is further illustrated, but never in any form the present invention is limited, and any conversion or the replacement based on training centre of the present invention, done, all belong to protection scope of the present invention.
The callable stone paper packaging vessel of easy degraded of the present invention comprise 0 ~ 100 part of weight part acrylic resin, 0 ~ 100 part PP stone paper special-purpose master batch, 0 ~ 10 part of Masterbatch, help 0 ~ 10 part of 0 ~ 2 part of degradation agents and moisture absorption master batch.
Described acrylic resin is homo-polypropylene, and melt flow rate (MFR) is 2.5 ~ 3.5g/10min.
The special-purpose master batch of described PP stone paper is degradable master batch.
Described degradable master batch is to be processed by the inorganic mineral powder of weight percent 75 ~ 85%, 15 ~ 19% acrylic resin, 0.1 ~ 0.3% help degradation agents, 0.4 ~ 0.6% titanium dioxide, 0.5 ~ 1.5% coupling agent and 1.1 ~ 1.5% lubricant.
Described degradable master batch is to be processed by the inorganic mineral powder of weight percent 80%, 17% acrylic resin, 0.2% help degradation agents, 0.5% titanium dioxide, 1% coupling agent and 1.3% lubricant.The purpose of using is to substitute the synthetic macromolecule resin of making of petroleum resources, reduces costs, and promotes photodegradation.
Described Masterbatch is the painted concentrated master batch of food grade polyolefine or food grade toner.
The described degradation agents that helps is low temperature-controlled thermooxidative degradation additive and/or photodegradable aid.
Described moisture absorption master batch is for take the moisture absorption master batch that inorganic oxide is carrier as the major ingredient polyolefine.
The preparation method of the callable stone paper packaging vessel of easy degraded of the present invention comprises pre-treatment, preparation process, specifically comprises:
A, pre-treatment: by heavily weighing of formula, mix drying;
B, preparation: the raw material after pre-treatment is heated and extruded diaphragm and introduce under molten state that plastics suction mould carries out plastic uptake and cooling forming obtains target compound.
The described drying of A step is for joining load weighted raw material respectively in drying blendor dry 1 ~ 2h under 60 ~ 120 ℃.
The B step is described to be prepared as the raw material after pre-treatment is extruded through heating, press polish, cooling and shaping, is wound into sheet material by sheet extruder, again sheet material is sent into and inhaled/rush in molding machine, send to and inhale/rush the mould district and inhaled/rush and mould through heating into molten again, through cooling and shaping, the demoulding, obtain target compound.
If produce the packaging vessel with Food Contact, preferably adopt multi-layer co-extruded sheet material unit, extexine and internal skin adopt brand new polypropylene, middle level adopts 0~100 part of acrylic resin, 0~10 part of PP Masterbatch, help 0~2 part of degradation agents, 0~10 part of moisture absorption master batch, 0~100 part of the special-purpose master batch of stone paper, guarantee that the product hygienic standard meets the GB18006.1-2009 related request.
Below with the preparation of PP stone paper packaging vessel so that principle of work of the present invention is described, the preparation of PP stone paper packaging vessel comprises the following steps:
By 0~100 part of acrylic resin, 0~10 part of PP Masterbatch, help 0~2 part of degradation agents, 0~10 part of moisture absorption master batch, and 0~100 part of the special-purpose master batch of stone paper joins respectively in drying blendor at the temperature of 60~120 ℃ dry 1~2 hour.
(2) preparation method of PP stone paper packaging vessel:
1) curtain coating plastics sucking moulding method claims again single stage method to make
To pour in the forcing machine feed bin of curtain coating plastic uptake unit through super-dry, the material that mixes, regulate and control each phase technological temperature at 135~170 ℃, after being heated to design temperature, be incubated 15~30 minutes, slowly adjusting screw(rod) rotating speed to 60~90 rev/mins.After running well, adjust temperature to 130~160 ℃, the startup Packing Machine is rotated, about per minute 32~40 moulds of adjusting rotary speed, but adjust the Packing Machine velocity of rotation or adjust grammes per square metre adjustment die head temperature and the horizontal local thickness degree of die gap controlling diaphragm sheet that screw speed can be controlled Blister product.Diaphragm to be extruded is adjusted intact, after conforming to quality requirements, can be by still in the Packing Machine that the diaphragm of molten state is rotating, start the plastic uptake switch, make it by the mold shape plastics sucking moulding, then through operations such as stamping-out, stamping-out, arrangement, check, sterilization, packings, be PP stone paper packaging vessel product.
2) sheet material (punching) method of moulding of inhaling claims again two step method to make:
Step 1: batch mixing drying treatment
By 0~100 part of acrylic resin, 0~10 part of PP Masterbatch, help 0~2 part of degradation agents, 0~10 part of moisture absorption master batch, and 0~100 part of the special-purpose master batch of stone paper joins respectively in drying blendor at the temperature of 60~120 ℃ dry 1~2 hour.
Step 2: the making of stone paper sheet material
The material mixed is poured in the hopper of calendered sheet unit, regulated and controled each phase temperature and be controlled between 135~210 ℃, after being heated to design temperature, be incubated 15~30 minutes, slow adjusting screw(rod) rotating speed to 200~450 rev/mins.After running well, adjust temperature to 135~180 ℃, notice that the main control system electric current is between 180A~220A, melt pressure is controlled at 4~9Mpa, at 3~20 rev/mins, (annotate: sheet material thickness degree reaches to set and requires rear its feeding rotating speed must keep constant regulation and control metering feeding screw speed, to guarantee the uniform and stable property of extrusion capacity.) adjust two gaps between stack to control sheet material transverse integral thickness degree and calendering smooth finish, adjust T die head die gap to control the horizontal local thickness degree of sheet material.Treat that the extrusion sheet adjustment is intact, cut both sides, the adjustment sheet width can be introduced sheet material in winder after meeting the Packing Machine requirement, is rolled up sheet material products.
Step 3: the making of packaging vessel product
Sheet material is put on the unwinding rack of suction (punching) molding machine, sheet material is introduced to the traction of inhaling (punching) molding machine presses in chain, regulation and control suctions (punching) are moulded the heated die plate temperature and are about 160 ℃~250 ℃, regulation and control are inhaled (punching) and are moulded the vacuum time delay 1~4 second, during cooling fixed response time 2~5 seconds, then start and inhale the running of (punching) molding machine, make sheet material be inhaled into the die for molding of (or pouring) setting when being heated into molten state, again through cooling and shaping, the demoulding, severing.Then send into stamping-out in clicker press machine and become goods, more become PP stone paper packaging vessel product through check, sterilization, packing.
Embodiment 1---produce the 10ml oyster white medicine holder of calcium carbonate content 45%, every grammes per square metre 5 grams.
By 33 parts of acrylic resins, 3 parts of white master batches, help 2 parts of degradation agentss, 2 parts of moisture absorption master batches, and 60 parts of the special-purpose master batches of stone paper, join respectively in drying blendor at the temperature of 60~120 ℃ dry 1~2 hour.To pour in the forcing machine feed bin of curtain coating plastic uptake unit through super-dry, the material that mixes again, regulate and control each phase technological temperature at 145~160 ℃, after being heated to design temperature, be incubated 20 minutes, slowly adjusting screw(rod) rotating speed to 80 rev/min.After the extruded material that runs well, adjustment is carried out inching to each phase temperature, starting Packing Machine rotates, about per minute 36 moulds of adjusting rotary speed, but adjustment Packing Machine velocity of rotation or adjustment screw speed can be controlled, the grammes per square metre of Blister product is adjusted die head temperature and the horizontal local thickness degree of die gap controlling diaphragm sheet is even.Diaphragm to be extruded is adjusted intact, after conforming to quality requirements, can be by still in the Packing Machine that the diaphragm of molten state is rotating, start the plastic uptake switch, make it by the mold shape plastics sucking moulding, the grammes per square metre that Packing Machine velocity of rotation or the holder of screw speed control 10ml oyster white medicine are adjusted in sampling is about 5 grams ± 1 gram, then by every four moulds, cuts off work in-process, sends into through the clicker press machine stamping-out and is finished product, is the holder of PP stone paper 10ml oyster white medicine through operations such as arrangement, check, sterilization, packings again.
Embodiment 2---produce the oyster white mess-tin of calcium carbonate content 64%, every grammes per square metre 20 grams.
By 14 parts of acrylic resins, 3 parts of white master batches, help 1 part of degradation agents, 2 parts of moisture absorption master batches, and 80 parts of the special-purpose master batches of stone paper, join respectively in drying blendor at the temperature of 60~120 ℃ dry 1~2 hour.The material mixed is poured in the hopper of calendered sheet unit, regulated and controled each phase temperature and be controlled between 160~180 ℃, after being heated to design temperature, be incubated 30 minutes, slowly adjusting screw(rod) rotating speed to 400 rev/min.After running well, adjust temperature to 135~160 ℃, notice that the main control system electric current is between 210A, melt pressure is controlled at 6~8Mpa, at 16 rev/mins, (annotate: sheet material thickness degree reaches to set and requires rear its feeding rotating speed must keep constant regulation and control metering feeding screw speed, to guarantee the uniform and stable property of extrusion capacity.), adjusting clearance control sheet material transverse integral thickness degree between two stacks is 0.50mm, adjusts the pulling speed of two stacks at 14.2~14.5 m/mins, adjusts T die head die gap, controls the horizontal local thickness degree deviation of sheet material at ± 0.02mm.Treat that the extrusion sheet adjustment is intact, cut both sides, the adjustment sheet width can be introduced sheet material in winder after meeting the Packing Machine requirement, is rolled up sheet material products.Again sheet material is put on the unwinding rack of Packing Machine, and sheet material is introduced in the traction pressure chain of Packing Machine, regulation and control plastic uptake heated die plate temperature is about 215 ℃, regulation and control plastic uptake vacuum time delay 3.5 seconds, during cooling fixed response time 4 seconds, then start the Packing Machine running, make sheet material be inhaled into the die for molding of setting when being heated into molten state, again through cooling and shaping, the demoulding, severing.Then send into stamping-out in clicker press machine and become goods, more become PP stone paper oyster white mess-tin product through check, sterilization, packing.
Embodiment 3---produce calcium carbonate content 25%, the oyster white 002 type rice bowl of every grammes per square metre 7 grams.
By 65 parts of acrylic resins, 3 parts of white master batches, help 1 part of degradation agents, 2 parts of moisture absorption master batches, and 30 parts of the special-purpose master batches of stone paper, join respectively in drying blendor at the temperature of 60~120 ℃ dry 1~2 hour.The material mixed is poured in the hopper of HSJP-90X matrix material unit again, regulated and controled each phase technological temperature and be controlled between 140~175 ℃, after being heated to above-mentioned design temperature, be incubated 30 minutes, open main frame, slowly speed governing to 80 rev/min.The main control system electric current is between 70~90A, adjusting clearance control sheet material transverse integral thickness degree between two stacks is 0.45mm, adjust the pulling speed of two stacks at 16 m/mins, adjust T die head die gap, control the horizontal local thickness degree deviation of sheet material at ± 0.02mm.Treat that the extrusion sheet adjustment is intact, cut both sides, the adjustment sheet width can be introduced sheet material in winder after meeting the Packing Machine requirement, is rolled up sheet material products.Sheet material is put on the unwinding rack that rushes molding machine again, and sheet material is introduced to the traction of rushing molding machine and press in chain, the regulation and control punching is moulded the heated die plate temperature and is about 200 ℃, regulate the air compressor machine air pressure 8kg/cm2 that qi of chong channel ascending adversely is used, per minute 22 moulds are moulded in the regulation and control punching, make sheet material be washed into the die for molding stamping-out of setting and blow out goods when being heated into molten state, then pick up, check, sterilize, pack through inspection and become oyster white 002 type rice bowl.
Test example 1
By the photodegradation test observation, embodiment 1 test-results is as follows:
Test example 2
By the photodegradation test observation, embodiment 2 test-results are as follows:
Test example 3
By the photodegradation test observation, embodiment 3 test-results are as follows: