WO2021098034A1 - Salt floating equipment and method for removing lifting grip or handle of waste edible oil bottle (can) - Google Patents
Salt floating equipment and method for removing lifting grip or handle of waste edible oil bottle (can) Download PDFInfo
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- WO2021098034A1 WO2021098034A1 PCT/CN2020/071944 CN2020071944W WO2021098034A1 WO 2021098034 A1 WO2021098034 A1 WO 2021098034A1 CN 2020071944 W CN2020071944 W CN 2020071944W WO 2021098034 A1 WO2021098034 A1 WO 2021098034A1
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- Prior art keywords
- sinking
- floating
- floating material
- motor
- hinge
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- 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
- B29B17/02—Separating plastics from other materials
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- 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
- B29B17/02—Separating plastics from other materials
- B29B2017/0203—Separating plastics from plastics
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- 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
- B29B17/02—Separating plastics from other materials
- B29B2017/0213—Specific separating techniques
- B29B2017/0217—Mechanical separating techniques; devices therefor
- B29B2017/0237—Mechanical separating techniques; devices therefor using density difference
- B29B2017/0244—Mechanical separating techniques; devices therefor using density difference in liquids
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- 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
Definitions
- the invention relates to the technical field of food packaging, in particular to a salt bleaching device and a method for removing handles and handles of waste edible oil bottles (pots).
- Polyester (PET) bottles are the main force in food and beverage packaging.
- the world's annual production of polyester bottles is about 30 million tons, of which China is about 6 million tons.
- the old polyester bottles after consumption are extremely chemically inert and difficult to degrade under natural conditions, which not only causes a great burden on the global environment, but also causes a great waste of resources. Recycling polyester waste is of great significance for solving resource shortages, reducing the development of primary resources, reducing waste emissions, and achieving sustainable development.
- polyester bottle flakes which are then used as raw materials for reuse, such as spinning recycled polyester fibers, food packaging, and so on.
- the old polyester bottles have passed the market circulation, they have been polluted to a certain extent, mixed with impurities such as metal and sand; the old polyester bottles themselves have mixed colors, and most of the bottle attachments such as caps, handles, handles, and labels are non-polymerized.
- Ester material: PVC and PP plastic bottles are easily mixed in polyester (PET) bottles because of the same shape and color, and there are many difficulties in cleaning and processing.
- PET polyester
- Edible oil bottles including vegetable oils such as golden dragon oil, soy sauce packaging bottles (pots), etc.
- the material of the bottle (pot) is mainly polyester (PET), and the materials of the handle and handle are ABS, PE, PP, PS, etc.
- the materials are complex and the density varies, and there is no certain rule for selection.
- the handle is embedded in the bottle (pot), which is very difficult to handle.
- the technical problem to be solved by the present invention is to provide a method for removing handles and handles of waste edible oil bottles (pots).
- the method provided by the present invention can separate polyester materials (bottle flakes) without manual separation.
- the handles, handles and other non-polyester materials are effectively separated, and the separation effect is good.
- the present invention provides a salt bleaching device, including:
- a material dispersing device used to disperse the materials sent into the flotation separation tank and a dispersing motor driving the device;
- Floating material advancing hinge used to push the floating material in the flotation separation tank to the floating material discharging hinge, and a floating material advancing motor used to drive the floating material advancing hinge;
- Floating material discharging hinge used to send the floating material out of the device and the floating material discharging motor used to drive the floating material discharging hinge;
- the sinker advancing hinge used to push the sinking material in the flotation separation tank to the sinker discharging hinge, and the sinker advancing motor used to drive the sinker advancing hinge;
- a sinking material discharging hinge used to send the sinking material out of the device and a sinking material discharging motor used to drive the sinking material discharging hinge.
- the discharge end of the feed auger is connected with the material inlet of the flotation separation tank, and is obliquely pressed on the top edge of the flotation separation tank.
- the floating material propelling hinged dragons are arranged side by side on the upper part of the flotation separation tank; the floating material propelling hinged dragons are in three rows; the rotation direction of the spiral blades of the floating material propelling hinged dragons in the middle row and the direction of both sides in contrast.
- the floating material propelling motor is arranged on the side wall of the flotation separation tank; the floating material discharging hinge is connected with the floating material outlet of the flotation separation tank, and is arranged obliquely on the side wall of the flotation separation tank.
- both sides of the top of the flotation separation tank are respectively provided with a material inlet and a float outlet, and the bottom is provided with a sinker outlet.
- the sinking material propelling motor and the floating material advancing motor are arranged on opposite sides; the sinking material advancing hinged dragon is in a row; the sinking material advancing hinged dragon pushes the sinking material to the sinking material outlet; the sinking material The discharging hinge dragon is connected with the sinking material outlet.
- the present invention provides a method for removing handles and handles of waste edible oil bottles (jugs) by using the salt bleaching device according to any one of the above technical solutions, including:
- the handle and handle of the edible oil bottle (pot) are crushed and the salt bleaching liquid is mixed and placed in the flotation separation tank, and the material is dispersed by the material dispersing device, and the sinking and floating separation is carried out to obtain the sinking material and the floating material;
- the salt bleaching liquid is The mass ratio of water and industrial salt is 100:28;
- the sinking material is pushed to the sinking material discharging hinge through the sinking material advancing hinge driven by the sinking material advancing motor for discharging and recycling;
- the floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor.
- the power of the material dispersing motor is 1.5kw
- the power of the sinking propulsion motor is 2.2kw
- the power of the float propulsion motor is 2.2kw
- the power of the float discharging motor is 2.2kw
- the power of the sinking discharging motor is 1.5kw.
- the sink-float separation temperature is 25-35°C.
- the density of the salt bleaching liquid is 1.15-1.16.
- the present invention provides a method for removing the handle and handle of a waste edible oil bottle (kettle) by using the salt bleaching device according to any one of the above technical solutions, which includes: putting the edible oil bottle (kettle) The handle and handle are crushed and the salt bleaching liquid is mixed and placed in the flotation separation tank, and the material is scattered by the material dispersing device, and the sinking and floating separation is carried out to obtain the sinking material and the floating material; the salt bleaching liquid is water and the mass ratio of industrial salt is 100:28; the sinking material is pushed to the sinking discharging hinged dragon by the sinking material advancing hinged dragon driven by the sinking material advancing motor for discharging and recycling; the floating material is pushed to the floating material by the floating material advancing hinged dragon driven by the floating material advancing motor The discharging hinge dragon carries out discharging.
- the invention adopts a specific salt bleaching device combined with salt bleaching liquid to separate the PET and non-PET in the handle and handle of the edible oil bottle (kettle), which can achieve a good separation effect.
- the method is convenient to use, has no harm, and no pollution. , The separation cost is low.
- Figure 1 is a side view of the salt bleaching device of the present invention
- Figure 2 is a front view of the salt bleaching device of the present invention.
- Figure 3 is a top view of the salt bleaching device of the present invention.
- the present invention provides a salt bleaching device and a method for removing handles and handles of waste edible oil bottles (jugs).
- jugs waste edible oil bottles
- the present invention provides a salt bleaching device, including:
- a material dispersing device used to disperse the materials sent into the flotation separation tank and a dispersing motor driving the device;
- Floating material advancing hinge used to push the floating material in the flotation separation tank to the floating material discharging hinge, and a floating material advancing motor used to drive the floating material advancing hinge;
- Floating material discharging hinge used to send the floating material out of the device and the floating material discharging motor used to drive the floating material discharging hinge;
- the sinker advancing hinge used to push the sinking material in the flotation separation tank to the sinker discharging hinge, and the sinker advancing motor used to drive the sinker advancing hinge;
- a sinking material discharging hinge used to send the sinking material out of the device and a sinking material discharging motor used to drive the sinking material discharging hinge.
- the salt bleaching device provided by the present invention includes a flotation separation tank.
- the flotation separation tank of the present invention is the core component of the salt bleaching device, and is a place for salt bleaching and separation.
- the material of the flotation separation cell of the present invention is preferably stainless steel, and the length of the separation cell is 470 cm to 490; the width is 120 to 140 cm; and the height is 150 to 170 cm.
- the two sides of the top of the flotation separation tank of the present invention are respectively provided with a material inlet and a float outlet, and the bottom is provided with a sinking outlet.
- the salt bleaching device provided by the invention includes a material feeding auger for feeding the material into the flotation separation tank.
- the present invention does not limit the feed-in material hinged dragon, as long as the material is separated to the flotation separation tank conveyor belt; the feed-in material hinged dragon is at the bottom and the discharge end is at the top.
- the discharge end of the feed auger is connected with the material inlet of the flotation separation tank, and the discharge end is obliquely pressed on the top edge of the flotation separation tank.
- the salt bleaching device provided by the present invention includes a material dispersing device for dispersing the materials sent into the flotation separation tank and a dispersing motor for driving the device.
- the present invention does not limit the dispersing motor that drives the device, as long as it is well known to those skilled in the art.
- the power of the material dispersing motor of the present invention is preferably 1.5kw.
- the material dispersing device of the present invention disperses the materials entering the salt bleaching device, which can improve the ups and downs effect.
- the salt bleaching device provided by the present invention includes a floating material propelling hinge used to push the floating material in the flotation separation tank to the floating material discharging hinge and a floating material propelling motor used to drive the floating material propelling hinge.
- the floating material propelling hinges of the present invention are arranged side by side on the upper part of the flotation separation tank; the floating material propelling hinges are preferably in three rows; the rotation direction of the spiral blades of the floating material propelling hinges in the middle row and the direction on both sides in contrast. That is, the materials in the flotation tank reciprocate in the flotation separation tank through the floating material propelling hinged dragon, and finally from the floating material outlet to the floating material discharging hinged dragon.
- the spiral direction of the blades on the hinged dragon of the present invention is determined by the direction of material travel, the pipe axis is flat, and the tolerance perpendicular to the axis is not more than 1mm, the blades are welded firmly, and the welds are uniform, and the left and right shaft heads are modulated and processed HB230-250, left and right The shaft head is processed after welding.
- the floating material propelling hinged dragon can transfer the material that enters the sink and float separation tank with a density less than that of the salt floating on the surface. At the same time, the teeth of the hinged dragon can be further agitated to further help the sinking and floating separation.
- the floating material propelling motor used for driving the floating material propelling hinged dragon of the present invention is arranged on the side wall of the flotation separation tank.
- the power of the floating material propulsion motor of the present invention is preferably 2.2kw.
- the salt bleaching device provided by the present invention includes a floating material discharging hinge used to send the floating material out of the device and a floating material discharging motor used to drive the floating material discharging hinge.
- the floating material discharging hinge of the present invention is connected with the floating material outlet of the flotation separation tank, and is arranged obliquely on the side wall of the flotation separation tank.
- the power of the floating material discharging motor of the present invention is preferably 2.2kw.
- the floating material discharging hinged dragon of the present invention sends the floating material separated by salt bleaching out of the machine to go to the next process, which is a non-PET component.
- the salt bleaching device provided by the present invention includes a sinker advancing hinge used to push the sinking material in the flotation separation tank to the sinking material discharging hinge and a sinking material advancing motor used to drive the sinking advancing hinge.
- the sinking material propelling motor and the floating material propelling motor of the present invention are arranged on opposite sides. They are respectively arranged on both sides of the flotation separation tank, and the height does not need to be the same, it can be according to actual needs.
- the sinking material propelling hinged dragon of the present invention is preferably one row; it is arranged at the bottom of the flotation separation tank. The sinker advancing hinge dragon pushes the sinker to the sinker outlet.
- the sinking material propelling hinge of the present invention sinks the materials that enter the sink and float separation tank, and the materials with a density greater than the salt float density into the bottom of the machine for material transportation, and at the same time, the teeth of the hinge screw can be further agitated to further help the sink and float separation.
- the power of the sinker propulsion motor of the present invention is preferably 2.2kw.
- the salt bleaching device provided by the present invention includes a sinking material discharging hinge used to send the sinking material out of the device and a sinking material discharging motor used to drive the sinking material discharging hinge.
- the sinker discharge hinge of the present invention is connected with the sinker outlet.
- the power of the sinking material discharging motor of the present invention is preferably 1.5kw.
- the sinking and discharging hinge of the present invention can preferably be arranged obliquely from bottom to top, and the feeding end is set at the sinking outlet at the bottom of the flotation separation tank.
- the sinking material discharging hinge of the invention sends the sinking material after salt bleaching and separation out of the machine to go to the next process, which is a PET component and can be recycled.
- the ups and downs of PET and non-PET can be separated, which can achieve good results. This method is convenient to use, has no harm, no pollution, and low separation cost.
- Figures 1 to 3 The salt bleaching device in some of the preferred embodiments of the present invention is shown in Figures 1 to 3, wherein Figure 1 is a side view, Figure 2 is a front view, and Figure 3 is a top view.
- 1 is the material feeding hinge dragon and motor
- 2 is the material dispersing motor and dispersing device
- 3 is the sinking propulsion motor
- 4 is the floating material propelling and dispersing motor
- 5 is the floating material discharging hinge and floating device.
- Material discharging motor 6 is sinking discharging hinged dragon and sinking motor
- 7 flotation separation tank 8 floating material advancing hinged dragon
- 9 sinking material advancing hinged dragon 9 sinking material advancing hinged dragon.
- the present invention provides a method for removing handles and handles of waste edible oil bottles (jugs) by using the salt bleaching device according to any one of the above technical solutions, including:
- the handle and handle of the edible oil bottle (pot) are crushed and the salt bleaching liquid is mixed and placed in the flotation separation tank, and the material is dispersed by the material dispersing device, and the sinking and floating separation is carried out to obtain the sinking material and the floating material;
- the salt bleaching liquid is The mass ratio of water and industrial salt is 100:28;
- the sinking material is pushed to the sinking material discharging hinge through the sinking material advancing hinge driven by the sinking material advancing motor for discharging and recycling;
- the floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor.
- the invention provides a method for removing the handle and handle of a waste edible oil bottle (kettle) by a salt bleaching device. First, the handle and handle of the edible oil bottle (kettle) are crushed.
- the existing cleaning oiler bottles are separated from other polyester bottles in different materials.
- Ordinary polyester bottles are mainly separated from PET and bottle cap PE and a small amount of label paper PVC.
- the density of each material that needs to be separated is different.
- the present invention first also includes pretreatment of the purchased oil bottle, and the pretreatment is preferably: unpacking, cleaning of the entire bottle, manual sorting, crushing, and cleaning into the hot pot.
- the present invention does not limit the unpacking, cleaning of the whole bottle, manual sorting, crushing, and cleaning into the hot pot, as long as those skilled in the art are well-known, the cleaning time of the whole bottle is preferably 8-10 minutes;
- the whole bottle cleaning temperature is preferably 85-95°C; more preferably 88-92°C;
- the hot washing time of the broken bottle flakes is preferably 20-25 min;
- the hot washing temperature of the broken bottle flakes is preferably 25-35°C;
- Hot-washing temperature of sheet hot pot 88 ⁇ 90°C (the temperature in the middle of hot-washing pot).
- the liquid level of the cleaning liquid of the whole bottle cleaning machine of the present invention 1/6; the filling level of the cleaning liquid of the hot washing machine: 3/5.
- the mesh size of the crushing is preferably 12-14 mm.
- the mass ratio of the salt bleaching liquid to water and industrial salt is 100:28; the density of the salt bleaching liquid is 1.15-1.16.
- the concentration of salt bleaching solution is formulated within the standard range (1.15-1.16) to keep the content of active ingredients stable, effectively improving and stabilizing the quality of regenerated bottle flakes.
- the PVC content of recycled bottle flakes is below 50PPM, a drop of about 100PPM, the label paper content is about 20PPM, a drop of 100PPM, and the PE content is about 30, a drop of 100PPM.
- the material is scattered by the material dispersing device, and the ups and downs are separated to obtain the sinking material and the floating material.
- the power of the material dispersing motor of the present invention is 1.5kw. Break up the materials entering the sink-floating machine to improve the sink-floating effect.
- the sinking material is pushed to the sinking material discharging hinge through the sinking material advancing hinge driven by the sinking material advancing motor for discharging and recycling;
- the power of the sinker propulsion motor is 2.2kw; the power of the sinker discharge motor is 1.5kw.
- the sink-float separation temperature is preferably 25-35°C.
- the materials entering the sink-floating separator the materials with the density of the material greater than the density of the liquid sink into the bottom of the flotation tank, and are driven by the screw auger driven by the motor to transport the sinking material forward; the sinking material is discharged by the screw auger, and the sinking and floating are separated.
- the sinking material is sent out of the machine, which is the PET component.
- the floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor.
- the power of the floating material propulsion motor of the present invention is 2.2kw; the power of the floating material discharging motor is 2.2kw.
- the material that enters the sink-floating separator of the present invention the material whose material density is less than the liquid density floats on the surface of the liquid, and is driven by the auger driven by the motor, so that the floating material is conveyed in the direction of the outlet; the floating material is discharged by the auger, and the floating material is separated after the sinking and floating The floating material is sent out of the machine to the next process.
- the crushed edible oil bottle (pot) together with its handle, handle and other materials are introduced into the salt bleaching tank (sinking and floating separation tank), and the salt bleaching liquid is evenly dispersed and pushed forward.
- the hand and handle materials float out, and the polyester material higher than this density is led out through the sinking discharge screw into the right process for cleaning and processing, and recycled polyester bottle flakes are obtained.
- the quality of recycled polyester flakes is significantly improved, and the non-PET content is reduced from more than 200ppm to less than 100ppm.
- Improve labor productivity Each ton of used edible oil bottles (pots) can save 15 yuan in labor costs.
- the present invention provides a method for removing the handle and handle of a waste edible oil bottle (kettle) by using the salt bleaching device according to any one of the above technical solutions.
- the method includes: crushing the handle and handle of the edible oil bottle (kettle) with salt.
- the bleaching liquid is mixed and placed in the flotation separation tank, and is dispersed by the material dispersing device, and the sinking and floating separation is carried out to obtain the sinking material and the floating material;
- the salt bleaching solution is water and industrial salt in a mass ratio of 100:28;
- the sinking material advancing hinged dragon driven by the sinking material advancing motor is pushed to the sinking material discharging hinge for discharging for recycling; the floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor .
- the invention uses a specific salt bleaching device combined with salt bleaching liquid to separate the PET and non-PET in the handle and handle of the edible oil bottle (kettle), which can achieve a good separation effect.
- the method is convenient to use, non-hazardous, and pollution-free. , The separation cost is low.
- a salt bleaching device and a method for removing the handle and handle of a waste edible oil bottle (kettle) provided by the present invention will be described in detail below with reference to embodiments.
- connection device of the present invention is
- Flotation separation tank both sides of the top of the flotation separation tank are respectively provided with a material inlet and a float outlet, and the bottom is provided with a sinking outlet.
- the floating material propulsion motor is arranged on the side wall of the flotation separation tank; the floating material discharging hinge is connected with the floating material outlet of the flotation separation tank, and is arranged obliquely on the side wall of the flotation separation tank; The floating material discharging hinge of the floating material discharging device and the floating material discharging motor used to drive the floating material discharging hinge; it is used to advance the sinking material in the flotation separation tank to the sinking material discharging hinge of the sinking material discharging hinge.
- a sinking dragon and a sinking propulsion motor for driving the sinking propulsion hinged dragon; the sinking propulsion motor and the floating material propelling motor are arranged on opposite sides; the sinking propelling hinged dragon is in a row; The propelling hinged dragon pushes the sinking material to the sinking material outlet; the sinking material discharging hinged dragon is connected with the sinking material outlet.
- Every 100 kg of water contains 28 kg of salt, and it is formulated into a salt bleaching liquid with a density (1.15-1.16)
- Crusher temperature room temperature
- Hot washing temperature for broken bottle flakes 88 ⁇ 90°C (the temperature in the middle of the hot washing pot).
- the filling level of the cleaning fluid of the hot washer 3/5.
- the feeding frequency is 18Hz, and the discharging frequency of each pot is separately controlled to 16HZ to obtain the soaking and cleaning effect of the bottle flakes.
- the added agent is recycled to dehydrate and rinse the bottle flakes, and the density is separated, dehydrated, rinsed, scrubbed, and dehydrated. , The finished bottle flakes.
- the mass ratio of salt bleaching liquid to water and industrial salt is 100:28; the density of salt bleaching liquid is 1.15 ⁇ 1.16; the sinking material is pushed to the sinking material discharging hinged dragon by the sinking material propulsion hinge dragon driven by the sinking material propulsion motor for discharging. Recycling; the floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor.
- the power of the material dispersing motor is 1.5kw
- the power of the sinking propulsion motor is 2.2kw
- the power of the floating material propulsion motor is 2.2kw
- the power of the floating material discharging motor is 2.2kw
- the sinking material is discharged
- the power of the feed motor is 1.5kw.
- Salt water rinsing time of broken bottles and flakes 30min
- salt water rinsing and separation tank temperature of broken bottles normal temperature
- liquid level of flotation separation tank to overflow (water recycling).
- Test results The content of non-PET is less than 100ppm, the cap material and the bottle flakes are fully separated; the PVC content of the recycled bottle flakes is below 50PPM, a drop of about 100PPM, the label paper content is about 20PPM, a drop of 100PPM, and the PE content is about 30. Drop 100PPM.
- Every 100 kg of water contains 20 kg of salt, and it is formulated into a salt bleaching liquid with a density (1.12-1.14)
- Crusher temperature room temperature
- Hot washing temperature for broken bottle flakes 88 ⁇ 90°C (the temperature in the middle of the hot washing pot).
- the filling level of the cleaning fluid of the hot washer 3/5.
- the feeding frequency is 18Hz, and the discharging frequency of each pot is separately controlled to 16HZ to obtain the soaking and cleaning effect of the bottle flakes.
- the added agent is recycled to dehydrate and rinse the bottle flakes, and the density is separated, dehydrated, rinsed, scrubbed, and dehydrated. , Finished bottle flakes
- the handle and handle of the edible oil bottle (jug) treated above are mixed with the salt bleaching liquid and mixed and placed in the flotation separation tank, and dispersed by the material dispersing device, and the sinking and floating are separated to obtain the sinking material and the floating material;
- the density of the salt bleaching liquid is 1.12-1.14; the sinking material is pushed to the sinking material discharging hinged dragon by the sinking material advancing hinge driven by the sinking material advancing motor for discharging and recycling; the floating material is propelled by the floating material driven by the floating material advancing motor
- the hinge dragon pushes to the floating material discharging hinge dragon for discharging.
- the power of the material dispersing motor is 1.5kw
- the power of the sinking propulsion motor is 2.2kw
- the power of the floating material propulsion motor is 2.2kw
- the power of the floating material discharging motor is 2.2kw
- the sinking material is discharged
- the power of the feed motor is 1.5kw.
- Salt water rinsing time of broken bottles and flakes 30min
- salt water rinsing and separation tank temperature of broken bottles normal temperature
- liquid level of flotation separation tank to overflow (water recycling).
- Test result The non-PET content reaches above 100ppm and below 300ppm, and a small amount of bottle cap material sinks into the bottle flake material.
- the PVC content of recycled bottle flakes is more than 50PPM, the label paper content is more than 20PPM, and the PE content is more than 30ppm.
- Every 100 kg of water contains 35 kg of salt, which is formulated into a salt bleaching liquid with a density (1.17-1.18)
- Crusher temperature room temperature
- Hot washing temperature for broken bottle flakes 88 ⁇ 90°C (the temperature in the middle of the hot washing pot).
- the filling level of the cleaning fluid of the hot washer 3/5.
- the feeding frequency is 18Hz, and the discharging frequency of each pot is separately controlled to 16HZ to obtain the soaking and cleaning effect of the bottle flakes.
- the added agent is recycled to dehydrate and rinse the bottle flakes, and the density is separated, dehydrated, rinsed, scrubbed, and dehydrated. , The finished bottle flakes;
- the handle and handle of the edible oil bottle (jug) treated above are mixed with the salt bleaching liquid and mixed and placed in the flotation separation tank, and dispersed by the material dispersing device, and the sinking and floating are separated to obtain the sinking material and the floating material;
- the density of the salt bleaching liquid is 1.17-1.18;
- the sinking material is pushed to the sinking material discharging hinged dragon by the sinking material advancing hinged dragon driven by the sinking material advancing motor for discharging and recycling;
- the floating material is propelled by the floating material driven by the floating material advancing motor
- the hinge dragon pushes to the floating material discharging hinge dragon for discharging.
- the power of the material dispersing motor is 1.5kw
- the power of the sinking propulsion motor is 2.2kw
- the power of the floating material propulsion motor is 2.2kw
- the power of the floating material discharging motor is 2.2kw
- the sinking material is discharged
- the power of the feed motor is 1.5kw.
- Salt water rinsing time of broken bottles and flakes 30min
- salt water rinsing and separation tank temperature of broken bottles normal temperature
- liquid level of flotation separation tank to overflow (water recycling).
- Test result The non-PET content is below 110ppm, but a small amount of flakes do not sink, and they enter the cap discharge screw together with the cap. That is: the bottle flakes cannot sink to the bottom of the salt bleaching liquid, causing difficulty in discharging at the bottom. A small number of flakes do not sink and enter the cap discharge screw together with the bottle cap, resulting in bottle flakes in the bottle cap material.
- Water as flotation fluid adjust the density by adjusting the temperature of the water.
- the density of water changes with temperature. Lowering the temperature can increase the density to increase the buoyancy for separation.
- the temperature of the water changes, and the density changes little, especially for some non-PET materials, the density is 1.05, and the density is only 0.999 when the water temperature is zero.
- the normal temperature of the water exceeds zero degrees. As a result, the above-mentioned flotation separation of PET and non-PET cannot be achieved.
- Sodium hydroxide is used as the flotation liquid: Sodium hydroxide is used to adjust the density. Through experiments, the density formulated with sodium hydroxide can achieve the effect of specific gravity separation. But the disadvantages: Sodium hydroxide is highly corrosive to equipment, unsafe for personnel to operate, and costly (7,000 yuan per ton), and it will increase the alkalinity of cleaning wastewater and increase the cost of sewage treatment.
- Potassium carbonate is highly hygroscopic, and can absorb carbon dioxide and moisture when exposed to the air, making it difficult to store and use. The cost is also high, the price is 6,500 yuan per ton.
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- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
A method for removing a lifting grip or a handle of a waste edible oil bottle (can) using salt floating equipment, comprising: crushing a lifting grip or a handle of an edible oil bottle (can), mixing same with a salt floating liquid, placing the mixture in a floating separation pool, dispersing same by a material dispersing device, and performing sinking-floating separation to obtain a sinking material and a floating material, the salt floating liquid comprising water and industrial salt in a mass ratio of 100:28; pushing the sinking material to a sinking material discharging auger conveyor by a sinking material pushing auger conveyor driven by a sinking material pushing motor for discharging and recycling; and pushing the floating material to a floating material discharging auger conveyor by a floating material pushing auger conveyor driven by a floating material pushing motor for discharging. By using the specific salt floating equipment in combination with a salt floating liquid to perform sinking-floating separation on PET and non-PET materials in lifting grips or handles of edible oil bottles (cans), a good separation effect can be achieved; the present method is convenient to use, nonharmful, pollution-free, and low in separation cost.
Description
本申请要求于2019年11月22日提交中国专利局、申请号为201911154433.1、发明名称为“一种盐漂装置和去除废旧食用油瓶(壶)提手、手柄的方法”的中国专利申请的优先权,其全部内容通过引用结合在本申请中。This application requires a Chinese patent application filed with the Chinese Patent Office on November 22, 2019, the application number is 201911154433.1, and the invention title is "a salt bleaching device and a method for removing the handle and handle of a waste edible oil bottle (kettle)". Priority, the entire content of which is incorporated in this application by reference.
本发明涉及食品包装技术领域,尤其是涉及一种盐漂装置和去除废旧食用油瓶(壶)提手、手柄的方法。The invention relates to the technical field of food packaging, in particular to a salt bleaching device and a method for removing handles and handles of waste edible oil bottles (pots).
聚酯(PET)瓶是食品、饮料包装的主力军,世界年生产聚酯瓶约3000万吨,其中中国约600万吨。消费后的旧聚酯瓶具有极强的化学惰性,很难在自然条件下降解,不仅对地球环境造成很大的负担,而且还会造成极大的资源浪费。将聚酯废料循环再利用,对解决资源短缺、减少原生资源的开发,减少废物排放,实现可持续发展具有重要意义。Polyester (PET) bottles are the main force in food and beverage packaging. The world's annual production of polyester bottles is about 30 million tons, of which China is about 6 million tons. The old polyester bottles after consumption are extremely chemically inert and difficult to degrade under natural conditions, which not only causes a great burden on the global environment, but also causes a great waste of resources. Recycling polyester waste is of great significance for solving resource shortages, reducing the development of primary resources, reducing waste emissions, and achieving sustainable development.
当前,对旧聚酯瓶回收再利用,首先是对其进行清洗加工,生产成再生聚酯瓶片,然后作为再利用的原料,如纺制再生聚酯纤维、食品包装等。但由于旧聚酯瓶已经过市场流通,受到一定污染,混有金属、泥沙等杂质;旧聚酯瓶本身存在颜色杂,盖、提手、手柄、标签等瓶体附着物多为非聚酯材料;PVC、PP材质的塑料瓶因形状颜色相同,极易混杂在聚酯(PET)瓶中,清洗加工存在许多困难。生产的再生聚酯瓶片,产品档次低,质量稳定性差、产品质量不高:影响后续循环再利用。At present, the recycling and reuse of old polyester bottles is first to clean and process them to produce recycled polyester bottle flakes, which are then used as raw materials for reuse, such as spinning recycled polyester fibers, food packaging, and so on. However, because the old polyester bottles have passed the market circulation, they have been polluted to a certain extent, mixed with impurities such as metal and sand; the old polyester bottles themselves have mixed colors, and most of the bottle attachments such as caps, handles, handles, and labels are non-polymerized. Ester material: PVC and PP plastic bottles are easily mixed in polyester (PET) bottles because of the same shape and color, and there are many difficulties in cleaning and processing. The recycled polyester bottle flakes produced have low product grades, poor quality stability, and low product quality: affecting subsequent recycling and reuse.
对旧聚酯瓶进行清洗加工,成为生产再生聚酯纤维的原料,是目前最为主要的资源再利用方式。在中国,由于饮食习惯,旧聚酯瓶中食用油瓶(壶)的比例较大,大概占到15-20%。Cleaning and processing the old polyester bottles to become the raw material for the production of recycled polyester fibers is currently the most important resource reuse method. In China, due to eating habits, the proportion of edible oil bottles (pots) in old polyester bottles is relatively large, accounting for about 15-20%.
食用油瓶(壶),包括菜油如金龙油、酱油的包装用瓶(壶)等都是带有手柄或提手的。瓶(壶)的材质主要是聚酯(PET),而提手、手柄的材质分别有ABS、PE、PP、PS等,材质复杂,密度不一,挑选没有一定的规律。且手柄是镶嵌在瓶(壶)中,处理十分困难。Edible oil bottles (pots), including vegetable oils such as golden dragon oil, soy sauce packaging bottles (pots), etc., are all equipped with handles or handles. The material of the bottle (pot) is mainly polyester (PET), and the materials of the handle and handle are ABS, PE, PP, PS, etc. The materials are complex and the density varies, and there is no certain rule for selection. And the handle is embedded in the bottle (pot), which is very difficult to handle.
目前在对废旧食用油瓶(壶)加工处理过程中,需将手柄、提手与瓶(壶)彻底分离,现有的操作办法主要是利用人工把手柄撬掉,剪刀把提手剪去,费时费力,而且还处理不干净,影响再生聚酯瓶片的质量。At present, in the process of processing waste edible oil bottles (pots), it is necessary to completely separate the handle, handle and bottle (pot). The existing operation method is mainly to manually pry off the handle and cut the handle with scissors. It is time-consuming and labor-intensive, and the handling is not clean, which affects the quality of recycled polyester bottle flakes.
发明内容Summary of the invention
有鉴于此,本发明要解决的技术问题在于提供一种去除废旧食用油瓶(壶)提手、手柄的方法,本发明提供的方法无需先进行人工分离即可将聚酯材料(瓶片)的提手、手柄等非聚酯类材料有效分离出来,分离效果好。In view of this, the technical problem to be solved by the present invention is to provide a method for removing handles and handles of waste edible oil bottles (pots). The method provided by the present invention can separate polyester materials (bottle flakes) without manual separation. The handles, handles and other non-polyester materials are effectively separated, and the separation effect is good.
本发明提供了一种盐漂装置,包括:The present invention provides a salt bleaching device, including:
浮选分离池;Flotation separation tank;
用于将物料送入浮选分离池的送入物料绞龙;Feeding auger for feeding materials into the flotation separation tank;
用于将送入浮选分离池的物料打散的物料打散装置和驱动所述装置的打散电机;A material dispersing device used to disperse the materials sent into the flotation separation tank and a dispersing motor driving the device;
用于将浮选分离池中浮料推进至浮料出料铰龙的浮料推进铰龙和用于驱动所述浮料推进铰龙的浮料推进电机;Floating material advancing hinge used to push the floating material in the flotation separation tank to the floating material discharging hinge, and a floating material advancing motor used to drive the floating material advancing hinge;
用于将浮料送出装置的浮料出料铰龙和用于驱动浮料出料铰龙的浮料出料电机;Floating material discharging hinge used to send the floating material out of the device and the floating material discharging motor used to drive the floating material discharging hinge;
用于将浮选分离池中沉料推进至沉料出料铰龙的沉料推进铰龙和用于驱动所述沉料推进铰龙的沉料推进电机;The sinker advancing hinge used to push the sinking material in the flotation separation tank to the sinker discharging hinge, and the sinker advancing motor used to drive the sinker advancing hinge;
用于将沉料送出装置的沉料出料铰龙和用于驱动所述沉料出料铰龙的沉料出料电机。A sinking material discharging hinge used to send the sinking material out of the device and a sinking material discharging motor used to drive the sinking material discharging hinge.
优选的,所述送入物料绞龙出料端与所述浮选分离池物料入口相连,倾斜压制于所述浮选分离池顶部边缘。Preferably, the discharge end of the feed auger is connected with the material inlet of the flotation separation tank, and is obliquely pressed on the top edge of the flotation separation tank.
优选的,所述浮料推进铰龙并排设置于所述浮选分离池上部;所述浮料推进铰龙为3排;中间排浮料推进铰龙的螺旋叶片的旋向与两侧的方向相反。Preferably, the floating material propelling hinged dragons are arranged side by side on the upper part of the flotation separation tank; the floating material propelling hinged dragons are in three rows; the rotation direction of the spiral blades of the floating material propelling hinged dragons in the middle row and the direction of both sides in contrast.
优选的,所述浮料推进电机设置于所述浮选分离池侧壁;所述浮料出料铰龙与浮选分离池浮料出口相连,倾斜设置于所述浮选分离池侧壁。Preferably, the floating material propelling motor is arranged on the side wall of the flotation separation tank; the floating material discharging hinge is connected with the floating material outlet of the flotation separation tank, and is arranged obliquely on the side wall of the flotation separation tank.
优选的,所述浮选分离池顶部两侧分别设置有物料入口和浮料出口, 底部设置有沉料出口。Preferably, both sides of the top of the flotation separation tank are respectively provided with a material inlet and a float outlet, and the bottom is provided with a sinker outlet.
优选的,所述沉料推进电机与所述浮料推进电机呈相对侧设置;所述沉料推进铰龙为1排;沉料推进铰龙将沉料推送至沉料出口;所述沉料出料铰龙与所述沉料出口相连。Preferably, the sinking material propelling motor and the floating material advancing motor are arranged on opposite sides; the sinking material advancing hinged dragon is in a row; the sinking material advancing hinged dragon pushes the sinking material to the sinking material outlet; the sinking material The discharging hinge dragon is connected with the sinking material outlet.
本发明提供了一种采用上述技术方案任意一项所述的盐漂装置去除废旧食用油瓶(壶)提手、手柄的方法,包括:The present invention provides a method for removing handles and handles of waste edible oil bottles (jugs) by using the salt bleaching device according to any one of the above technical solutions, including:
将食用油瓶(壶)提手、手柄粉碎与盐漂液混合置于浮选分离池中,经过物料打散装置打散,进行沉浮分离,得到沉料和浮料;所述盐漂液为水和工业盐质量比为100:28;The handle and handle of the edible oil bottle (pot) are crushed and the salt bleaching liquid is mixed and placed in the flotation separation tank, and the material is dispersed by the material dispersing device, and the sinking and floating separation is carried out to obtain the sinking material and the floating material; the salt bleaching liquid is The mass ratio of water and industrial salt is 100:28;
沉料经沉料推进电机驱动的沉料推进铰龙推送至沉料出料铰龙进行出料进行回收;The sinking material is pushed to the sinking material discharging hinge through the sinking material advancing hinge driven by the sinking material advancing motor for discharging and recycling;
浮料经浮料推进电机驱动的浮料推进铰龙推送至浮料出料铰龙进行出料。The floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor.
优选的,所述物料打散电机的功率为1.5kw,沉料推进电机的功率为2.2kw;所述浮料推进电机的功率为2.2kw;所述浮料出料电机的功率为2.2kw;所述沉料出料电机的功率为1.5kw。Preferably, the power of the material dispersing motor is 1.5kw, the power of the sinking propulsion motor is 2.2kw; the power of the float propulsion motor is 2.2kw; the power of the float discharging motor is 2.2kw; The power of the sinking discharging motor is 1.5kw.
优选的,所述沉浮分离温度为25~35℃。Preferably, the sink-float separation temperature is 25-35°C.
优选的,所述盐漂液的密度为1.15~1.16。Preferably, the density of the salt bleaching liquid is 1.15-1.16.
与现有技术相比,本发明提供了一种采用上述技术方案任意一项所述的盐漂装置去除废旧食用油瓶(壶)提手、手柄的方法,包括:将食用油瓶(壶)提手、手柄粉碎与盐漂液混合置于浮选分离池中,经过物料打散装置打散,进行沉浮分离,得到沉料和浮料;所述盐漂液为水和工业盐质量比为100:28;沉料经沉料推进电机驱动的沉料推进铰龙推送至沉料出料铰龙进行出料进行回收;浮料经浮料推进电机驱动的浮料推进铰龙推送至浮料出料铰龙进行出料。本发明采用特定的盐漂装置结合盐漂液对食用油瓶(壶)提手、手柄中PET和非PET进行沉浮分离,能够达到良好的分离效果,本方法使用方便,没有危害性,无污染,分离成本低。Compared with the prior art, the present invention provides a method for removing the handle and handle of a waste edible oil bottle (kettle) by using the salt bleaching device according to any one of the above technical solutions, which includes: putting the edible oil bottle (kettle) The handle and handle are crushed and the salt bleaching liquid is mixed and placed in the flotation separation tank, and the material is scattered by the material dispersing device, and the sinking and floating separation is carried out to obtain the sinking material and the floating material; the salt bleaching liquid is water and the mass ratio of industrial salt is 100:28; the sinking material is pushed to the sinking discharging hinged dragon by the sinking material advancing hinged dragon driven by the sinking material advancing motor for discharging and recycling; the floating material is pushed to the floating material by the floating material advancing hinged dragon driven by the floating material advancing motor The discharging hinge dragon carries out discharging. The invention adopts a specific salt bleaching device combined with salt bleaching liquid to separate the PET and non-PET in the handle and handle of the edible oil bottle (kettle), which can achieve a good separation effect. The method is convenient to use, has no harm, and no pollution. , The separation cost is low.
图1为本发明盐漂装置侧视图;Figure 1 is a side view of the salt bleaching device of the present invention;
图2为本发明盐漂装置正视图;Figure 2 is a front view of the salt bleaching device of the present invention;
图3为本发明盐漂装置俯视图。Figure 3 is a top view of the salt bleaching device of the present invention.
本发明提供了一种盐漂装置和去除废旧食用油瓶(壶)提手、手柄的方法,本领域技术人员可以借鉴本文内容,适当改进工艺参数实现。特别需要指出的是,所有类似的替换和改动对本领域技术人员来说是显而易见的,它们都属于本发明保护的范围。本发明的方法及应用已经通过较佳实施例进行了描述,相关人员明显能在不脱离本发明内容、精神和范围内对本文的方法和应用进行改动或适当变更与组合,来实现和应用本发明技术。The present invention provides a salt bleaching device and a method for removing handles and handles of waste edible oil bottles (jugs). Those skilled in the art can learn from the content of this article and appropriately improve the process parameters. In particular, it should be pointed out that all similar replacements and modifications are obvious to those skilled in the art, and they all fall within the protection scope of the present invention. The method and application of the present invention have been described through the preferred embodiments. It is obvious that relevant personnel can modify or appropriately change and combine the methods and applications herein without departing from the content, spirit and scope of the present invention to realize and apply the present invention. Invent technology.
本发明提供了一种盐漂装置,包括:The present invention provides a salt bleaching device, including:
浮选分离池;Flotation separation tank;
用于将物料送入浮选分离池的送入物料绞龙;Feeding auger for feeding materials into the flotation separation tank;
用于将送入浮选分离池的物料打散的物料打散装置和驱动所述装置的打散电机;A material dispersing device used to disperse the materials sent into the flotation separation tank and a dispersing motor driving the device;
用于将浮选分离池中浮料推进至浮料出料铰龙的浮料推进铰龙和用于驱动所述浮料推进铰龙的浮料推进电机;Floating material advancing hinge used to push the floating material in the flotation separation tank to the floating material discharging hinge, and a floating material advancing motor used to drive the floating material advancing hinge;
用于将浮料送出装置的浮料出料铰龙和用于驱动浮料出料铰龙的浮料出料电机;Floating material discharging hinge used to send the floating material out of the device and the floating material discharging motor used to drive the floating material discharging hinge;
用于将浮选分离池中沉料推进至沉料出料铰龙的沉料推进铰龙和用于驱动所述沉料推进铰龙的沉料推进电机;The sinker advancing hinge used to push the sinking material in the flotation separation tank to the sinker discharging hinge, and the sinker advancing motor used to drive the sinker advancing hinge;
用于将沉料送出装置的沉料出料铰龙和用于驱动所述沉料出料铰龙的沉料出料电机。A sinking material discharging hinge used to send the sinking material out of the device and a sinking material discharging motor used to drive the sinking material discharging hinge.
本发明提供的盐漂装置包括浮选分离池。The salt bleaching device provided by the present invention includes a flotation separation tank.
本发明所述浮选分离池为盐漂装置的核心部件,是进行盐漂分离的场所。The flotation separation tank of the present invention is the core component of the salt bleaching device, and is a place for salt bleaching and separation.
本发明所述浮选分离池的材质优选为不锈钢,所述分离池的长为470cm~490;宽度为120~140cm;高度为150~170cm。The material of the flotation separation cell of the present invention is preferably stainless steel, and the length of the separation cell is 470 cm to 490; the width is 120 to 140 cm; and the height is 150 to 170 cm.
本发明所述浮选分离池顶部两侧分别设置有物料入口和浮料出口,底 部设置有沉料出口。The two sides of the top of the flotation separation tank of the present invention are respectively provided with a material inlet and a float outlet, and the bottom is provided with a sinking outlet.
本发明提供的盐漂装置包括用于将物料送入浮选分离池的送入物料绞龙。The salt bleaching device provided by the invention includes a material feeding auger for feeding the material into the flotation separation tank.
本发明对于所述送入物料铰龙不进行限定,向浮选分离池输送带分离物料即可;所述送入物料铰龙入料端在下,出料端在上。其中,所述送入物料绞龙出料端与所述浮选分离池物料入口相连,出料端倾斜压制于所述浮选分离池顶部边缘。The present invention does not limit the feed-in material hinged dragon, as long as the material is separated to the flotation separation tank conveyor belt; the feed-in material hinged dragon is at the bottom and the discharge end is at the top. Wherein, the discharge end of the feed auger is connected with the material inlet of the flotation separation tank, and the discharge end is obliquely pressed on the top edge of the flotation separation tank.
本发明提供的盐漂装置包括用于将送入浮选分离池的物料打散的物料打散装置和驱动所述装置的打散电机。The salt bleaching device provided by the present invention includes a material dispersing device for dispersing the materials sent into the flotation separation tank and a dispersing motor for driving the device.
本发明对于所述驱动所述装置的打散电机不进行限定,本领域技术人员熟知的即可。本发明所述物料打散电机的功率优选为1.5kw。The present invention does not limit the dispersing motor that drives the device, as long as it is well known to those skilled in the art. The power of the material dispersing motor of the present invention is preferably 1.5kw.
本发明所述物料打散装置把进入盐漂装置的物料打散,可以提高沉浮效果。The material dispersing device of the present invention disperses the materials entering the salt bleaching device, which can improve the ups and downs effect.
本发明提供的盐漂装置包括用于将浮选分离池中浮料推进至浮料出料铰龙的浮料推进铰龙和用于驱动所述浮料推进铰龙的浮料推进电机。The salt bleaching device provided by the present invention includes a floating material propelling hinge used to push the floating material in the flotation separation tank to the floating material discharging hinge and a floating material propelling motor used to drive the floating material propelling hinge.
本发明所述浮料推进铰龙并排设置于所述浮选分离池上部;所述浮料推进铰龙优选为3排;中间排浮料推进铰龙的螺旋叶片的旋向与两侧的方向相反。即为浮选池的物料经过浮料推进铰龙往复于所述浮选分离池,最终由浮料出口至浮料出料铰龙。The floating material propelling hinges of the present invention are arranged side by side on the upper part of the flotation separation tank; the floating material propelling hinges are preferably in three rows; the rotation direction of the spiral blades of the floating material propelling hinges in the middle row and the direction on both sides in contrast. That is, the materials in the flotation tank reciprocate in the flotation separation tank through the floating material propelling hinged dragon, and finally from the floating material outlet to the floating material discharging hinged dragon.
本发明铰龙上的叶片的螺旋方向由物料行进方向决定,管轴切面平整,与轴心垂直公差不大于1mm,叶片焊接牢固,且焊缝均匀一致,左右轴头调制处理HB230~250,左右轴头焊后加工。The spiral direction of the blades on the hinged dragon of the present invention is determined by the direction of material travel, the pipe axis is flat, and the tolerance perpendicular to the axis is not more than 1mm, the blades are welded firmly, and the welds are uniform, and the left and right shaft heads are modulated and processed HB230-250, left and right The shaft head is processed after welding.
上述浮料推进铰龙可以将进入沉浮分离池的物料小于盐漂密度浮在表面的物料传送,同时铰龙的齿牙可以进一步进行搅动从而进一步帮助沉浮分离。The floating material propelling hinged dragon can transfer the material that enters the sink and float separation tank with a density less than that of the salt floating on the surface. At the same time, the teeth of the hinged dragon can be further agitated to further help the sinking and floating separation.
本发明所述用于驱动所述浮料推进铰龙的浮料推进电机设置于所述浮选分离池侧壁。本发明所述浮料推进电机的功率优选为2.2kw。The floating material propelling motor used for driving the floating material propelling hinged dragon of the present invention is arranged on the side wall of the flotation separation tank. The power of the floating material propulsion motor of the present invention is preferably 2.2kw.
本发明提供的盐漂装置包括用于将浮料送出装置的浮料出料铰龙和用于驱动浮料出料铰龙的浮料出料电机。The salt bleaching device provided by the present invention includes a floating material discharging hinge used to send the floating material out of the device and a floating material discharging motor used to drive the floating material discharging hinge.
本发明所述浮料出料铰龙与浮选分离池浮料出口相连,倾斜设置于所述浮选分离池侧壁。The floating material discharging hinge of the present invention is connected with the floating material outlet of the flotation separation tank, and is arranged obliquely on the side wall of the flotation separation tank.
本发明所述浮料出料电机的功率优选为2.2kw。The power of the floating material discharging motor of the present invention is preferably 2.2kw.
本发明浮料出料铰龙把经过盐漂分离后的浮料送出机器,去下道工序,即为非PET组分。The floating material discharging hinged dragon of the present invention sends the floating material separated by salt bleaching out of the machine to go to the next process, which is a non-PET component.
本发明提供的盐漂装置包括用于将浮选分离池中沉料推进至沉料出料铰龙的沉料推进铰龙和用于驱动所述沉料推进铰龙的沉料推进电机。The salt bleaching device provided by the present invention includes a sinker advancing hinge used to push the sinking material in the flotation separation tank to the sinking material discharging hinge and a sinking material advancing motor used to drive the sinking advancing hinge.
本发明所述沉料推进电机与所述浮料推进电机呈相对侧设置。分别设置于所述浮选分离池的两侧,高度无需一致,根据实际需求即可。The sinking material propelling motor and the floating material propelling motor of the present invention are arranged on opposite sides. They are respectively arranged on both sides of the flotation separation tank, and the height does not need to be the same, it can be according to actual needs.
本发明所述沉料推进铰龙优选为1排;设置于浮选分离池底部。沉料推进铰龙将沉料推送至沉料出口。The sinking material propelling hinged dragon of the present invention is preferably one row; it is arranged at the bottom of the flotation separation tank. The sinker advancing hinge dragon pushes the sinker to the sinker outlet.
本发明沉料推进铰龙把进入沉浮分离池中的物料,大于盐漂密度的物料沉入机器底部物料输送,同时铰龙的齿牙可以进一步进行搅动从而进一步帮助沉浮分离。The sinking material propelling hinge of the present invention sinks the materials that enter the sink and float separation tank, and the materials with a density greater than the salt float density into the bottom of the machine for material transportation, and at the same time, the teeth of the hinge screw can be further agitated to further help the sink and float separation.
本发明所述沉料推进电机功率优选为2.2kw。The power of the sinker propulsion motor of the present invention is preferably 2.2kw.
本发明提供的盐漂装置包括用于将沉料送出装置的沉料出料铰龙和用于驱动所述沉料出料铰龙的沉料出料电机。The salt bleaching device provided by the present invention includes a sinking material discharging hinge used to send the sinking material out of the device and a sinking material discharging motor used to drive the sinking material discharging hinge.
本发明所述沉料出料铰龙与所述沉料出口相连。本发明所述沉料出料电机的功率优选为1.5kw。The sinker discharge hinge of the present invention is connected with the sinker outlet. The power of the sinking material discharging motor of the present invention is preferably 1.5kw.
本发明所述沉料出料铰龙优选可以为由下而上倾斜设置,入料端设置于所述浮选分离池底部沉料出口。The sinking and discharging hinge of the present invention can preferably be arranged obliquely from bottom to top, and the feeding end is set at the sinking outlet at the bottom of the flotation separation tank.
本发明沉料出料铰龙把经过盐漂分离后的沉料送出机器,去下一道工序,此为PET组分,可以进行回收利用。The sinking material discharging hinge of the invention sends the sinking material after salt bleaching and separation out of the machine to go to the next process, which is a PET component and can be recycled.
本发明人创造性的针对现有人工去除油壶提手、把手提供了一种新的盐漂装置,可以用于油壶的分离,以及PET的回收,PET和非PET进行沉浮分离,能够达到良好的分离效果,本方法使用方便,没有危害性,无污染,分离成本低。The inventor creatively provides a new salt bleaching device for the existing manual removal of oil can handles and handles, which can be used for the separation of oil cans and the recycling of PET. The ups and downs of PET and non-PET can be separated, which can achieve good results. This method is convenient to use, has no harm, no pollution, and low separation cost.
本发明其中一部分优选实施方式中盐漂装置如图1~3所示,其中图1为侧视图,图2为正视图,图3为俯视图。The salt bleaching device in some of the preferred embodiments of the present invention is shown in Figures 1 to 3, wherein Figure 1 is a side view, Figure 2 is a front view, and Figure 3 is a top view.
其中,1物料的进料铰龙和电机,,2为物料打散电机和打散装置,3为沉料推进电机,4为浮料推进打散电机,5为浮料出料铰龙和浮料出料电机,6为沉料出料铰龙和沉料电机,7浮选分离池,8浮料推进铰龙,9沉料推进铰龙。Among them, 1 is the material feeding hinge dragon and motor, 2 is the material dispersing motor and dispersing device, 3 is the sinking propulsion motor, 4 is the floating material propelling and dispersing motor, and 5 is the floating material discharging hinge and floating device. Material discharging motor, 6 is sinking discharging hinged dragon and sinking motor, 7 flotation separation tank, 8 floating material advancing hinged dragon, 9 sinking material advancing hinged dragon.
本发明提供了一种采用上述技术方案任意一项所述的盐漂装置去除废旧食用油瓶(壶)提手、手柄的方法,包括:The present invention provides a method for removing handles and handles of waste edible oil bottles (jugs) by using the salt bleaching device according to any one of the above technical solutions, including:
将食用油瓶(壶)提手、手柄粉碎与盐漂液混合置于浮选分离池中,经过物料打散装置打散,进行沉浮分离,得到沉料和浮料;所述盐漂液为水和工业盐质量比为100:28;The handle and handle of the edible oil bottle (pot) are crushed and the salt bleaching liquid is mixed and placed in the flotation separation tank, and the material is dispersed by the material dispersing device, and the sinking and floating separation is carried out to obtain the sinking material and the floating material; the salt bleaching liquid is The mass ratio of water and industrial salt is 100:28;
沉料经沉料推进电机驱动的沉料推进铰龙推送至沉料出料铰龙进行出料进行回收;The sinking material is pushed to the sinking material discharging hinge through the sinking material advancing hinge driven by the sinking material advancing motor for discharging and recycling;
浮料经浮料推进电机驱动的浮料推进铰龙推送至浮料出料铰龙进行出料。The floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor.
本发明提供了盐漂装置去除废旧食用油瓶(壶)提手、手柄的方法首先将食用油瓶(壶)提手、手柄粉碎。The invention provides a method for removing the handle and handle of a waste edible oil bottle (kettle) by a salt bleaching device. First, the handle and handle of the edible oil bottle (kettle) are crushed.
现有的清洗油壶瓶与其他聚酯瓶所要分离的材质不一样,普通聚酯瓶,主要是PET和瓶盖PE及少量标签纸PVC进行分离。而油壶瓶,要分离的有PE、PVC、ABS、PP、PS等。而每种需要分离的材料的密度是不一样的。The existing cleaning oiler bottles are separated from other polyester bottles in different materials. Ordinary polyester bottles are mainly separated from PET and bottle cap PE and a small amount of label paper PVC. And the oil can bottle, there are PE, PVC, ABS, PP, PS, etc. to be separated. The density of each material that needs to be separated is different.
本发明首先还包括将收购油壶瓶预处理,所述预处理优选为:解包、整瓶清洗、人工分选、破碎、进入热锅的清洗。The present invention first also includes pretreatment of the purchased oil bottle, and the pretreatment is preferably: unpacking, cleaning of the entire bottle, manual sorting, crushing, and cleaning into the hot pot.
本发明对于所述解包、整瓶清洗、人工分选、破碎、进入热锅的清洗不进行限定,本领域技术人员熟知的即可,所述整瓶清洗时间优选为8~10min;所述整瓶清洗温度优选为85~95℃;更优选为88~92℃;所述碎瓶片热洗时间优选为20~25min;所述碎瓶片热洗温度优选为25~35℃;碎瓶片热锅热洗温度:88~90℃(热洗锅中部温度)。本发明整瓶清洗机清洗液液位:1/6;热洗机清洗液装入液位:3/5。The present invention does not limit the unpacking, cleaning of the whole bottle, manual sorting, crushing, and cleaning into the hot pot, as long as those skilled in the art are well-known, the cleaning time of the whole bottle is preferably 8-10 minutes; The whole bottle cleaning temperature is preferably 85-95°C; more preferably 88-92°C; the hot washing time of the broken bottle flakes is preferably 20-25 min; the hot washing temperature of the broken bottle flakes is preferably 25-35°C; Hot-washing temperature of sheet hot pot: 88~90℃ (the temperature in the middle of hot-washing pot). The liquid level of the cleaning liquid of the whole bottle cleaning machine of the present invention: 1/6; the filling level of the cleaning liquid of the hot washing machine: 3/5.
所述粉碎的目数优选为12-14mm。The mesh size of the crushing is preferably 12-14 mm.
预处理完毕,粉碎后,与盐漂液混合置于浮选分离池中。After the pretreatment is completed, after crushing, it is mixed with the salt bleaching liquid and placed in the flotation separation tank.
按照本发明,所述盐漂液为水和工业盐质量比为100:28;所述盐漂液的密度为1.15~1.16。According to the present invention, the mass ratio of the salt bleaching liquid to water and industrial salt is 100:28; the density of the salt bleaching liquid is 1.15-1.16.
盐漂液浓度配制在标准范围内(1.15-1.16),使其有效成分含量保持稳定,有效提高和稳定再生瓶片品质。再生瓶片的PVC含量在50PPM以下,下降100PPM左右,标签纸含量20PPM左右,下降100PPM,PE含量30左右,下降100PPM。The concentration of salt bleaching solution is formulated within the standard range (1.15-1.16) to keep the content of active ingredients stable, effectively improving and stabilizing the quality of regenerated bottle flakes. The PVC content of recycled bottle flakes is below 50PPM, a drop of about 100PPM, the label paper content is about 20PPM, a drop of 100PPM, and the PE content is about 30, a drop of 100PPM.
本发明在实验中,使用工业盐调节密度。适量的工业盐加水,配置的分离液密度达到分离的效果。使用方便,没有危害性,价格便宜,每吨500元,成品料成本降低。达到PET和非PET分离效果的分离液密度要求。In the experiment of the present invention, industrial salt is used to adjust the density. Add water to the appropriate amount of industrial salt, and the density of the configured separation liquid can achieve the separation effect. It is easy to use, non-hazardous, low in price, 500 yuan per ton, and the cost of finished materials is reduced. Meet the separation liquid density requirement of PET and non-PET separation effect.
在浮选分离池中经过物料打散装置打散,进行沉浮分离,得到沉料和浮料。In the flotation separation tank, the material is scattered by the material dispersing device, and the ups and downs are separated to obtain the sinking material and the floating material.
本发明所述物料打散电机的功率为1.5kw。把进入沉浮机的物料打散,提高沉浮效果。The power of the material dispersing motor of the present invention is 1.5kw. Break up the materials entering the sink-floating machine to improve the sink-floating effect.
沉料经沉料推进电机驱动的沉料推进铰龙推送至沉料出料铰龙进行出料进行回收;The sinking material is pushed to the sinking material discharging hinge through the sinking material advancing hinge driven by the sinking material advancing motor for discharging and recycling;
按照本发明,沉料推进电机的功率为2.2kw;所述沉料出料电机的功率为1.5kw。According to the present invention, the power of the sinker propulsion motor is 2.2kw; the power of the sinker discharge motor is 1.5kw.
所述沉浮分离温度优选为25~35℃。The sink-float separation temperature is preferably 25-35°C.
进入沉浮分离机中的物料,物料密度大于液体密度的物料沉入浮选池底部,被电机驱动的绞龙带动,使沉料往前输送;沉料出料绞龙,把经过沉浮分离后的沉料送出机器,即为PET组分。The materials entering the sink-floating separator, the materials with the density of the material greater than the density of the liquid sink into the bottom of the flotation tank, and are driven by the screw auger driven by the motor to transport the sinking material forward; the sinking material is discharged by the screw auger, and the sinking and floating are separated. The sinking material is sent out of the machine, which is the PET component.
浮料经浮料推进电机驱动的浮料推进铰龙推送至浮料出料铰龙进行出料。The floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor.
本发明所述浮料推进电机的功率为2.2kw;所述浮料出料电机的功率为2.2kw。The power of the floating material propulsion motor of the present invention is 2.2kw; the power of the floating material discharging motor is 2.2kw.
本发明进入沉浮分离机中的物料,物料密度小于液体密度的物料浮在液体表面,被电机驱动的绞龙带动,使浮料往出口方向传送;浮料出料绞龙,把经过沉浮分离后的浮料送出机器,去下道工序。The material that enters the sink-floating separator of the present invention, the material whose material density is less than the liquid density floats on the surface of the liquid, and is driven by the auger driven by the motor, so that the floating material is conveyed in the direction of the outlet; the floating material is discharged by the auger, and the floating material is separated after the sinking and floating The floating material is sent out of the machine to the next process.
即为:本发明将经粉碎的食用油瓶(壶)连同其提手、手柄等材料导入盐漂槽(沉浮分离池),在盐漂液中均匀打散、推进,低于这个密度的提手、手柄材质漂浮出去,高于这个密度的聚酯材料通过沉料出料螺旋引出进入正道工序进行清洗加工,得到再生聚酯瓶片。将经粉碎混杂中聚酯材料(瓶片)的提手、手柄等非聚酯类材料有效分离出来,再生聚酯瓶片的品质明显提高,非PET含量从200ppm以上,降到了100ppm以内。提高劳动生产效率。每处理一吨旧食用油瓶(壶)可节约15元的劳动力成本。That is: in the present invention, the crushed edible oil bottle (pot) together with its handle, handle and other materials are introduced into the salt bleaching tank (sinking and floating separation tank), and the salt bleaching liquid is evenly dispersed and pushed forward. The hand and handle materials float out, and the polyester material higher than this density is led out through the sinking discharge screw into the right process for cleaning and processing, and recycled polyester bottle flakes are obtained. Effectively separate the handles and handles of polyester materials (bottle flakes) and other non-polyester materials in the pulverized mixture. The quality of recycled polyester flakes is significantly improved, and the non-PET content is reduced from more than 200ppm to less than 100ppm. Improve labor productivity. Each ton of used edible oil bottles (pots) can save 15 yuan in labor costs.
本发明提供了一种采用上述技术方案任意一项所述的盐漂装置去除废旧食用油瓶(壶)提手、手柄的方法,包括:将食用油瓶(壶)提手、手柄粉碎与盐漂液混合置于浮选分离池中,经过物料打散装置打散,进行沉浮分离,得到沉料和浮料;所述盐漂液为水和工业盐质量比为100:28;沉料经沉料推进电机驱动的沉料推进铰龙推送至沉料出料铰龙进行出料进行回收;浮料经浮料推进电机驱动的浮料推进铰龙推送至浮料出料铰龙进行出料。本发明采用特定的盐漂装置结合盐漂液对食用油瓶(壶)提手、手柄中PET和非PET进行沉浮分离,能够达到良好的分离效果,本方法使用方便,没有危害性,无污染,分离成本低。The present invention provides a method for removing the handle and handle of a waste edible oil bottle (kettle) by using the salt bleaching device according to any one of the above technical solutions. The method includes: crushing the handle and handle of the edible oil bottle (kettle) with salt. The bleaching liquid is mixed and placed in the flotation separation tank, and is dispersed by the material dispersing device, and the sinking and floating separation is carried out to obtain the sinking material and the floating material; the salt bleaching solution is water and industrial salt in a mass ratio of 100:28; The sinking material advancing hinged dragon driven by the sinking material advancing motor is pushed to the sinking material discharging hinge for discharging for recycling; the floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor . The invention uses a specific salt bleaching device combined with salt bleaching liquid to separate the PET and non-PET in the handle and handle of the edible oil bottle (kettle), which can achieve a good separation effect. The method is convenient to use, non-hazardous, and pollution-free. , The separation cost is low.
为了进一步说明本发明,以下结合实施例对本发明提供的一种盐漂装置和去除废旧食用油瓶(壶)提手、手柄的方法进行详细描述。In order to further illustrate the present invention, a salt bleaching device and a method for removing the handle and handle of a waste edible oil bottle (kettle) provided by the present invention will be described in detail below with reference to embodiments.
实施例1Example 1
按照本发明所述连接装置:According to the connection device of the present invention:
浮选分离池;所述浮选分离池顶部两侧分别设置有物料入口和浮料出口,底部设置有沉料出口。用于将物料送入浮选分离池的送入物料绞龙;送入物料绞龙出料端与所述浮选分离池物料入口相连,倾斜压制于所述浮选分离池顶部边缘;用于将送入浮选分离池的物料打散的物料打散装置和驱动所述装置的打散电机;用于将浮选分离池中浮料推进至浮料出料铰龙的浮料推进铰龙和用于驱动所述浮料推进铰龙的浮料推进电机;所述浮料推进铰龙并排设置于所述浮选分离池上部;所述浮料推进铰龙为3排;中间排浮料推进铰龙的螺旋叶片的旋向与两侧的方向相反。所述浮料推进电 机设置于所述浮选分离池侧壁;所述浮料出料铰龙与浮选分离池浮料出口相连,倾斜设置于所述浮选分离池侧壁;用于将浮料送出装置的浮料出料铰龙和用于驱动浮料出料铰龙的浮料出料电机;用于将浮选分离池中沉料推进至沉料出料铰龙的沉料推进铰龙和用于驱动所述沉料推进铰龙的沉料推进电机;所述沉料推进电机与所述浮料推进电机呈相对侧设置;所述沉料推进铰龙为1排;沉料推进铰龙将沉料推送至沉料出口;所述沉料出料铰龙与所述沉料出口相连。用于将沉料送出装置的沉料出料铰龙和用于驱动所述沉料出料铰龙的沉料出料电机。Flotation separation tank; both sides of the top of the flotation separation tank are respectively provided with a material inlet and a float outlet, and the bottom is provided with a sinking outlet. A feed auger for feeding materials into the flotation separation tank; the discharge end of the feed auger is connected with the material inlet of the flotation separation tank, and is inclined and pressed on the top edge of the flotation separation tank; A material dispersing device for dispersing materials sent into the flotation separation tank and a dispersing motor driving the device; a floating material advancing hinge used to push the floating material in the flotation separation tank to the floating material discharging hinge And a floating material propulsion motor for driving the floating material propelling hinged dragon; the floating material propelling hinged dragon is arranged side by side on the upper part of the flotation separation tank; the floating material propelling hinged dragon has 3 rows; the floating material is discharged in the middle The direction of rotation of the spiral blades of the propelling dragon is opposite to the direction on both sides. The floating material propulsion motor is arranged on the side wall of the flotation separation tank; the floating material discharging hinge is connected with the floating material outlet of the flotation separation tank, and is arranged obliquely on the side wall of the flotation separation tank; The floating material discharging hinge of the floating material discharging device and the floating material discharging motor used to drive the floating material discharging hinge; it is used to advance the sinking material in the flotation separation tank to the sinking material discharging hinge of the sinking material discharging hinge. A sinking dragon and a sinking propulsion motor for driving the sinking propulsion hinged dragon; the sinking propulsion motor and the floating material propelling motor are arranged on opposite sides; the sinking propelling hinged dragon is in a row; The propelling hinged dragon pushes the sinking material to the sinking material outlet; the sinking material discharging hinged dragon is connected with the sinking material outlet. A sinking material discharging hinge used to send the sinking material out of the device and a sinking material discharging motor used to drive the sinking material discharging hinge.
实施例2Example 2
将收购油壶瓶解包、整瓶清洗、人工分选、破碎、进入热锅的清洗、清洗后盐水漂洗进行深层分离Unpack the purchased oiler bottle, clean the whole bottle, manual sorting, crushing, cleaning into the hot pot, and brine rinsing after cleaning for deep separation
每100㎏水中,含盐28㎏,配制成密度(1.15-1.16)的盐漂液Every 100 kg of water contains 28 kg of salt, and it is formulated into a salt bleaching liquid with a density (1.15-1.16)
即清洗瓶片时,盐漂液的浓度为:水:盐:=100:28That is, when cleaning the bottle flakes, the concentration of the salt bleaching solution is: water: salt: = 100:28
1)停留时间1) Residence time
整瓶清洗时间:8~10minWashing time of the whole bottle: 8~10min
碎瓶片热洗时间:25minHot washing time for broken bottle flakes: 25min
2)清洗温度2) Cleaning temperature
整瓶清洗温度:90℃±2℃Whole bottle cleaning temperature: 90℃±2℃
粉碎机温度:常温Crusher temperature: room temperature
碎瓶片热洗温度:88~90℃(热洗锅中部温度)。Hot washing temperature for broken bottle flakes: 88~90℃ (the temperature in the middle of the hot washing pot).
3)液位3) Liquid level
整瓶清洗机清洗液液位:1/6Washing liquid level of the whole bottle washing machine: 1/6
热洗机清洗液装入液位:3/5。The filling level of the cleaning fluid of the hot washer: 3/5.
进料的频率为18Hz,每锅的出料频率分别控制为16HZ得到瓶片的浸泡清洗效果,加入的药剂循环使用,将瓶片脱水、漂洗,密度的分离、脱水、漂洗、搓洗、在脱水,成品瓶片。The feeding frequency is 18Hz, and the discharging frequency of each pot is separately controlled to 16HZ to obtain the soaking and cleaning effect of the bottle flakes. The added agent is recycled to dehydrate and rinse the bottle flakes, and the density is separated, dehydrated, rinsed, scrubbed, and dehydrated. , The finished bottle flakes.
4)盐漂:4) Salt bleaching:
将上述处理过的食用油瓶(壶)提手、手柄粉碎与盐漂液混合置于浮选分离池中,经过物料打散装置打散,进行沉浮分离,得到沉料和浮料; 所述盐漂液为水和工业盐质量比为100:28;盐漂液的密度为1.15~1.16;沉料经沉料推进电机驱动的沉料推进铰龙推送至沉料出料铰龙进行出料进行回收;浮料经浮料推进电机驱动的浮料推进铰龙推送至浮料出料铰龙进行出料。物料打散电机的功率为1.5kw,沉料推进电机的功率为2.2kw;所述浮料推进电机的功率为2.2kw;所述浮料出料电机的功率为2.2kw;所述沉料出料电机的功率为1.5kw。碎瓶片盐水漂洗时间:30min;碎瓶盐水漂洗分离池温度:常温;浮选分离池液位:至溢流口(水循环使用)。Mixing the handle and handle of the edible oil bottle (jug) treated above with the salt bleaching liquid in the flotation separation tank, and disperse the material through the material dispersing device, and carry out sinking and floating separation to obtain sinking material and floating material; The mass ratio of salt bleaching liquid to water and industrial salt is 100:28; the density of salt bleaching liquid is 1.15~1.16; the sinking material is pushed to the sinking material discharging hinged dragon by the sinking material propulsion hinge dragon driven by the sinking material propulsion motor for discharging. Recycling; the floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor. The power of the material dispersing motor is 1.5kw, the power of the sinking propulsion motor is 2.2kw; the power of the floating material propulsion motor is 2.2kw; the power of the floating material discharging motor is 2.2kw; the sinking material is discharged The power of the feed motor is 1.5kw. Salt water rinsing time of broken bottles and flakes: 30min; salt water rinsing and separation tank temperature of broken bottles: normal temperature; liquid level of flotation separation tank: to overflow (water recycling).
5)测试结果:非PET含量达到100ppm以内,瓶盖料和瓶片得到充分分离;再生瓶片的PVC含量在50PPM以下,下降100PPM左右,标签纸含量20PPM左右,下降100PPM,PE含量30左右,下降100PPM。5) Test results: The content of non-PET is less than 100ppm, the cap material and the bottle flakes are fully separated; the PVC content of the recycled bottle flakes is below 50PPM, a drop of about 100PPM, the label paper content is about 20PPM, a drop of 100PPM, and the PE content is about 30. Drop 100PPM.
对比例1Comparative example 1
将收购油壶瓶解包、材质分拣、整瓶清洗、人工分选、破碎、进入热锅的清洗、清洗后盐水漂洗进行深层分离Unpacking, material sorting, whole bottle cleaning, manual sorting, crushing, cleaning into the hot pot, and brine rinsing after cleaning for deep separation
每100㎏水中,含盐20㎏,配制成密度(1.12-1.14)的盐漂液Every 100 kg of water contains 20 kg of salt, and it is formulated into a salt bleaching liquid with a density (1.12-1.14)
即清洗瓶片时,盐漂液的浓度为:水:盐:=100:20That is, when cleaning the bottle flakes, the concentration of the salt bleaching solution is: water: salt: = 100:20
1)停留时间1) Residence time
整瓶清洗时间:8~10minWashing time of the whole bottle: 8~10min
碎瓶片热洗时间:25minHot washing time for broken bottle flakes: 25min
碎瓶片盐水漂洗时间:30minSalt water rinsing time of broken bottle flakes: 30min
2)清洗温度2) Cleaning temperature
整瓶清洗温度:90℃±2℃Whole bottle cleaning temperature: 90℃±2℃
粉碎机温度:常温Crusher temperature: room temperature
碎瓶片热洗温度:88~90℃(热洗锅中部温度)。Hot washing temperature for broken bottle flakes: 88~90℃ (the temperature in the middle of the hot washing pot).
3)液位3) Liquid level
整瓶清洗机清洗液液位:1/6Washing liquid level of the whole bottle washing machine: 1/6
热洗机清洗液装入液位:3/5。The filling level of the cleaning fluid of the hot washer: 3/5.
进料的频率为18Hz,每锅的出料频率分别控制为16HZ得到瓶片的浸泡清洗效果,加入的药剂循环使用,将瓶片脱水、漂洗,密度的分离、脱水、漂洗、搓洗、在脱水,成品瓶片The feeding frequency is 18Hz, and the discharging frequency of each pot is separately controlled to 16HZ to obtain the soaking and cleaning effect of the bottle flakes. The added agent is recycled to dehydrate and rinse the bottle flakes, and the density is separated, dehydrated, rinsed, scrubbed, and dehydrated. , Finished bottle flakes
4)盐漂:4) Salt bleaching:
将上述处理过的食用油瓶(壶)提手、手柄粉碎与盐漂液混合置于浮选分离池中,经过物料打散装置打散,进行沉浮分离,得到沉料和浮料;所述盐漂液的密度为1.12-1.14;沉料经沉料推进电机驱动的沉料推进铰龙推送至沉料出料铰龙进行出料进行回收;浮料经浮料推进电机驱动的浮料推进铰龙推送至浮料出料铰龙进行出料。物料打散电机的功率为1.5kw,沉料推进电机的功率为2.2kw;所述浮料推进电机的功率为2.2kw;所述浮料出料电机的功率为2.2kw;所述沉料出料电机的功率为1.5kw。碎瓶片盐水漂洗时间:30min;碎瓶盐水漂洗分离池温度:常温;浮选分离池液位:至溢流口(水循环使用)。The handle and handle of the edible oil bottle (jug) treated above are mixed with the salt bleaching liquid and mixed and placed in the flotation separation tank, and dispersed by the material dispersing device, and the sinking and floating are separated to obtain the sinking material and the floating material; The density of the salt bleaching liquid is 1.12-1.14; the sinking material is pushed to the sinking material discharging hinged dragon by the sinking material advancing hinge driven by the sinking material advancing motor for discharging and recycling; the floating material is propelled by the floating material driven by the floating material advancing motor The hinge dragon pushes to the floating material discharging hinge dragon for discharging. The power of the material dispersing motor is 1.5kw, the power of the sinking propulsion motor is 2.2kw; the power of the floating material propulsion motor is 2.2kw; the power of the floating material discharging motor is 2.2kw; the sinking material is discharged The power of the feed motor is 1.5kw. Salt water rinsing time of broken bottles and flakes: 30min; salt water rinsing and separation tank temperature of broken bottles: normal temperature; liquid level of flotation separation tank: to overflow (water recycling).
4)测试结果:非PET含量达到100ppm以上,300ppm以下,有少量瓶盖料下沉到瓶片料中。再生瓶片的PVC含量在50PPM以上,,标签纸含量20PPM以上,PE含量30ppm以上。4) Test result: The non-PET content reaches above 100ppm and below 300ppm, and a small amount of bottle cap material sinks into the bottle flake material. The PVC content of recycled bottle flakes is more than 50PPM, the label paper content is more than 20PPM, and the PE content is more than 30ppm.
对比例2Comparative example 2
将收购油壶瓶解包、材质分拣、整瓶清洗、人工分选、破碎、进入热锅的清洗、清洗后盐水漂洗进行深层分离Unpacking, material sorting, whole bottle cleaning, manual sorting, crushing, cleaning into the hot pot, and brine rinsing after cleaning for deep separation
每100㎏水中,含盐35㎏,配制成密度(1.17-1.18)的盐漂液Every 100 kg of water contains 35 kg of salt, which is formulated into a salt bleaching liquid with a density (1.17-1.18)
即清洗瓶片时,盐漂液的浓度为:水:盐:=100:35That is, when cleaning the bottle flakes, the concentration of the salt bleaching liquid is: water: salt: = 100:35
1)停留时间1) Residence time
整瓶清洗时间:8~10minWashing time of the whole bottle: 8~10min
碎瓶片热洗时间:25minHot washing time for broken bottle flakes: 25min
2)清洗温度2) Cleaning temperature
整瓶清洗温度:90℃±2℃Whole bottle cleaning temperature: 90℃±2℃
粉碎机温度:常温Crusher temperature: room temperature
碎瓶片热洗温度:88~90℃(热洗锅中部温度)。Hot washing temperature for broken bottle flakes: 88~90℃ (the temperature in the middle of the hot washing pot).
3)液位3) Liquid level
整瓶清洗机清洗液液位:1/6Washing liquid level of the whole bottle washing machine: 1/6
热洗机清洗液装入液位:3/5。The filling level of the cleaning fluid of the hot washer: 3/5.
进料的频率为18Hz,每锅的出料频率分别控制为16HZ得到瓶片的 浸泡清洗效果,加入的药剂循环使用,将瓶片脱水、漂洗,密度的分离、脱水、漂洗、搓洗、在脱水,成品瓶片;The feeding frequency is 18Hz, and the discharging frequency of each pot is separately controlled to 16HZ to obtain the soaking and cleaning effect of the bottle flakes. The added agent is recycled to dehydrate and rinse the bottle flakes, and the density is separated, dehydrated, rinsed, scrubbed, and dehydrated. , The finished bottle flakes;
4)盐漂:4) Salt bleaching:
将上述处理过的食用油瓶(壶)提手、手柄粉碎与盐漂液混合置于浮选分离池中,经过物料打散装置打散,进行沉浮分离,得到沉料和浮料;所述盐漂液的密度为1.17-1.18;沉料经沉料推进电机驱动的沉料推进铰龙推送至沉料出料铰龙进行出料进行回收;浮料经浮料推进电机驱动的浮料推进铰龙推送至浮料出料铰龙进行出料。物料打散电机的功率为1.5kw,沉料推进电机的功率为2.2kw;所述浮料推进电机的功率为2.2kw;所述浮料出料电机的功率为2.2kw;所述沉料出料电机的功率为1.5kw。碎瓶片盐水漂洗时间:30min;碎瓶盐水漂洗分离池温度:常温;浮选分离池液位:至溢流口(水循环使用)。The handle and handle of the edible oil bottle (jug) treated above are mixed with the salt bleaching liquid and mixed and placed in the flotation separation tank, and dispersed by the material dispersing device, and the sinking and floating are separated to obtain the sinking material and the floating material; The density of the salt bleaching liquid is 1.17-1.18; the sinking material is pushed to the sinking material discharging hinged dragon by the sinking material advancing hinged dragon driven by the sinking material advancing motor for discharging and recycling; the floating material is propelled by the floating material driven by the floating material advancing motor The hinge dragon pushes to the floating material discharging hinge dragon for discharging. The power of the material dispersing motor is 1.5kw, the power of the sinking propulsion motor is 2.2kw; the power of the floating material propulsion motor is 2.2kw; the power of the floating material discharging motor is 2.2kw; the sinking material is discharged The power of the feed motor is 1.5kw. Salt water rinsing time of broken bottles and flakes: 30min; salt water rinsing and separation tank temperature of broken bottles: normal temperature; liquid level of flotation separation tank: to overflow (water recycling).
5)测试结果:非PET含量达到110ppm以下,但是有少量片没有下沉,随瓶盖一起进入瓶盖出料螺旋。即为:瓶片料无法下沉到盐漂液底部,造成底部出料困难,有少量片没有下沉,随瓶盖一起进入瓶盖出料螺旋,造成瓶盖料里面有瓶片。5) Test result: The non-PET content is below 110ppm, but a small amount of flakes do not sink, and they enter the cap discharge screw together with the cap. That is: the bottle flakes cannot sink to the bottom of the salt bleaching liquid, causing difficulty in discharging at the bottom. A small number of flakes do not sink and enter the cap discharge screw together with the bottle cap, resulting in bottle flakes in the bottle cap material.
对比例3~5Comparative example 3~5
水作为浮选液:通过调节水的温度来调节密度。水的密度会随温度变化而变化,降低温度可增加密度,以增加浮力来进行分离。但是,经实验,水的温度变化,密度变化幅度不大,尤其是一些非PET材质,密度在1.05,水温在零度时密度也只有0.999。而生产过程中水的常温均超过零度。结果是无法实现上述PET和非PET的浮选分离。Water as flotation fluid: adjust the density by adjusting the temperature of the water. The density of water changes with temperature. Lowering the temperature can increase the density to increase the buoyancy for separation. However, through experiments, the temperature of the water changes, and the density changes little, especially for some non-PET materials, the density is 1.05, and the density is only 0.999 when the water temperature is zero. In the production process, the normal temperature of the water exceeds zero degrees. As a result, the above-mentioned flotation separation of PET and non-PET cannot be achieved.
采用氢氧化钠作为浮选液:采用氢氧化钠调节密度。经实验,用氢氧化钠调配的密度可以达到比重分离效果。但缺点:氢氧化钠对设备的腐蚀性较强,人员操作不安全,使用成本也高(每吨价格7000元),且会增加清洗废水的碱度,增加污水处理成本。Sodium hydroxide is used as the flotation liquid: Sodium hydroxide is used to adjust the density. Through experiments, the density formulated with sodium hydroxide can achieve the effect of specific gravity separation. But the disadvantages: Sodium hydroxide is highly corrosive to equipment, unsafe for personnel to operate, and costly (7,000 yuan per ton), and it will increase the alkalinity of cleaning wastewater and increase the cost of sewage treatment.
采用碳酸钾作为浮选液:碳酸钾吸湿性强,暴露在空气中能吸收二氧化碳和水分,不易保存和使用。成本也高,每吨价格6500元。Using potassium carbonate as the flotation fluid: Potassium carbonate is highly hygroscopic, and can absorb carbon dioxide and moisture when exposed to the air, making it difficult to store and use. The cost is also high, the price is 6,500 yuan per ton.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above are only the preferred embodiments of the present invention. It should be pointed out that for those of ordinary skill in the art, without departing from the principle of the present invention, several improvements and modifications can be made, and these improvements and modifications are also It should be regarded as the protection scope of the present invention.
Claims (10)
- 一种盐漂装置,其特征在于,包括:A salt bleaching device is characterized in that it comprises:浮选分离池;Flotation separation tank;用于将物料送入浮选分离池的送入物料绞龙;Feeding auger for feeding materials into the flotation separation tank;用于将送入浮选分离池的物料打散的物料打散装置和驱动所述装置的打散电机;A material dispersing device used to disperse the materials sent into the flotation separation tank and a dispersing motor driving the device;用于将浮选分离池中浮料推进至浮料出料铰龙的浮料推进铰龙和用于驱动所述浮料推进铰龙的浮料推进电机;Floating material advancing hinge used to push the floating material in the flotation separation tank to the floating material discharging hinge, and a floating material advancing motor used to drive the floating material advancing hinge;用于将浮料送出装置的浮料出料铰龙和用于驱动浮料出料铰龙的浮料出料电机;Floating material discharging hinge used to send the floating material out of the device and the floating material discharging motor used to drive the floating material discharging hinge;用于将浮选分离池中沉料推进至沉料出料铰龙的沉料推进铰龙和用于驱动所述沉料推进铰龙的沉料推进电机;The sinker advancing hinge used to push the sinking material in the flotation separation tank to the sinker discharging hinge, and the sinker advancing motor used to drive the sinker advancing hinge;用于将沉料送出装置的沉料出料铰龙和用于驱动所述沉料出料铰龙的沉料出料电机。A sinking material discharging hinge used to send the sinking material out of the device and a sinking material discharging motor used to drive the sinking material discharging hinge.
- 根据权利要求1所述的装置,其特征在于,所述送入物料绞龙出料端与所述浮选分离池物料入口相连,倾斜压制于所述浮选分离池顶部边缘。The device according to claim 1, characterized in that the discharge end of the feed auger is connected with the material inlet of the flotation separation tank, and is obliquely pressed on the top edge of the flotation separation tank.
- 根据权利要求1所述的装置,其特征在于,所述浮料推进铰龙并排设置于所述浮选分离池上部;所述浮料推进铰龙为3排;中间排浮料推进铰龙的螺旋叶片的旋向与两侧的方向相反。The device according to claim 1, wherein the floating material propelling hinged dragons are arranged side by side on the upper part of the flotation separation tank; the floating material propelling hinged dragons are in three rows; the floating material propelling hinged dragons of the middle row are arranged side by side. The direction of rotation of the spiral blade is opposite to the direction on both sides.
- 根据权利要求1所述的装置,其特征在于,所述浮料推进电机设置于所述浮选分离池侧壁;所述浮料出料铰龙与浮选分离池浮料出口相连,倾斜设置于所述浮选分离池侧壁。The device according to claim 1, wherein the floating material propulsion motor is arranged on the side wall of the flotation separation tank; the floating material discharging hinge is connected with the floating material outlet of the flotation separation tank, and is arranged obliquely On the side wall of the flotation separation tank.
- 根据权利要求1所述的装置,其特征在于,所述浮选分离池顶部两侧分别设置有物料入口和浮料出口,底部设置有沉料出口。The device according to claim 1, wherein the two sides of the top of the flotation separation tank are respectively provided with a material inlet and a floating material outlet, and the bottom is provided with a sinking material outlet.
- 根据权利要求1所述的装置,其特征在于,所述沉料推进电机与所述浮料推进电机呈相对侧设置;所述沉料推进铰龙为1排;沉料推进铰龙将沉料推送至沉料出口;所述沉料出料铰龙与所述沉料出口相连。The device according to claim 1, wherein the sinking material propulsion motor and the floating material advancing motor are arranged on opposite sides; the sinking material advancing hinged dragon is in a row; the sinking material advancing hinged dragon will sink the material Push to the sinker outlet; the sinker discharge hinge is connected with the sinker outlet.
- 一种采用权利要求1~6任意一项所述的盐漂装置去除废旧食用油瓶(壶)提手、手柄的方法,其特征在于,包括:A method for removing handles and handles of waste edible oil bottles (jugs) by using the salt bleaching device according to any one of claims 1 to 6, characterized in that it comprises:将食用油瓶(壶)提手、手柄粉碎与盐漂液混合置于浮选分离池中,经过物料打散装置打散,进行沉浮分离,得到沉料和浮料;所述盐漂液为水和工业盐质量比为100:28;The handle and handle of the edible oil bottle (pot) are crushed and the salt bleaching liquid is mixed and placed in the flotation separation tank, and the material is dispersed by the material dispersing device, and the sinking and floating separation is carried out to obtain the sinking material and the floating material; the salt bleaching liquid is The mass ratio of water and industrial salt is 100:28;沉料经沉料推进电机驱动的沉料推进铰龙推送至沉料出料铰龙进行出料进行回收;The sinking material is pushed to the sinking material discharging hinge through the sinking material advancing hinge driven by the sinking material advancing motor for discharging and recycling;浮料经浮料推进电机驱动的浮料推进铰龙推送至浮料出料铰龙进行出料。The floating material is pushed to the floating material discharging hinged dragon for discharging by the floating material advancing hinge driven by the floating material advancing motor.
- 根据权利要求7所述的方法,其特征在于,所述物料进料电机的功率2.2kw;物料打散电机的功率为1.5kw,沉料推进电机的功率为2.2kw;所述浮料推进电机的功率为2.2kw;所述浮料出料电机的功率为2.2kw;所述沉料出料电机的功率为1.5kw。The method according to claim 7, wherein the power of the material feeding motor is 2.2kw; the power of the material dispersing motor is 1.5kw, and the power of the sinking propulsion motor is 2.2kw; the floating material propulsion motor The power of the floating material discharge motor is 2.2kw; the power of the floating material discharge motor is 2.2kw; the power of the sinking material discharge motor is 1.5kw.
- 根据权利要求7所述的方法,其特征在于,所述沉浮分离温度为25~35℃。The method according to claim 7, wherein the sink-float separation temperature is 25-35°C.
- 根据权利要求7所述的方法,其特征在于,所述盐漂液的密度为1.15~1.16。The method according to claim 7, wherein the density of the salt bleaching liquid is 1.15-1.16.
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JP2000295964A (en) * | 1999-04-13 | 2000-10-24 | Matsushita Electric Ind Co Ltd | Device for purifying deteriorated oil |
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JP2000204391A (en) * | 1999-01-08 | 2000-07-25 | Matsushita Electric Ind Co Ltd | Apparatus for refining edible oil |
JP2000295964A (en) * | 1999-04-13 | 2000-10-24 | Matsushita Electric Ind Co Ltd | Device for purifying deteriorated oil |
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WO2007029111A1 (en) * | 2005-09-09 | 2007-03-15 | Cyclonic Systems & Technologies Sdn Bhd | Method and apparatus for separation and recovery of fruit, nut or vegetable oils from water, liquids and wastewater |
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