A method for co-disposing waste cosmetics using cement kilns

Abstract

The present invention relates to the technical field of waste cosmetics disposal, and specifically to a method for co-disposing waste cosmetics in a cement kiln; the waste cosmetics are transported into a shearing crusher for crushing, sieved through a drum screen after crushing, a metal solidifying dispersant is added to adsorb heavy metals, and sent to a sludge pool for treatment. After treatment, it is sent to incineration, and the slag is mixed with cement raw materials for calcination to obtain cement clinker. Most waste cosmetics packaging contains heavy metals, and general treatment will cause pollution. By adopting this method, waste cosmetics packaging can be effectively utilized, reducing pollution to the environment, while improving the production efficiency of cement kilns and the quality of cement products. In addition, since cement production is a process with high energy consumption, the use of waste cosmetics for calorific value recovery is also beneficial to energy conservation.

Description

Technical Field

[0001] The invention relates to the technical field of waste cosmetics disposal, in particular to a method for co-disposing waste cosmetics with a cement kiln. Background Art

[0002] With the rapid development of social economy, cosmetics have become a common consumer product in real life. Cosmetic bottles are a must in the cosmetics industry. Cosmetic bottles refer to a container that can isolate gas from the outside temperature or isolate external bacteria. There are glass bottles, plastic bottles, and PET bottles. Among them, the production of glass bottles consumes the most energy. More and more brands have proposed empty bottle recycling plans. For the premise of environmental protection, cosmetic bottles are recycled.

[0003] Patent No. CN114273002B discloses an environmentally friendly treatment device for cosmetic production waste, which relates to the field of cosmetic production technology. The present invention includes a base, a lifting movable frame, a crushing mechanism, a receiving mechanism and a swinging mechanism. Both sides of the base are detachably connected with a lifting movable frame. The other side of the base side seat plate is equipped with a crushing mechanism and a feeding mechanism. The feeding mechanism is installed directly below the crushing mechanism, and the discharging end of the feeding mechanism is equipped with a receiving mechanism. The inside of the receiving mechanism is equipped with a swinging mechanism. The receiving mechanism provided by the present invention has two material frames that can be used alternately. When the crushed waste bottle debris is unloaded, the crushed material collection will not be affected, and it is convenient to unload while collecting the material, thereby improving the collection efficiency. In addition, a lifting movable frame is provided, which is convenient to push the device to move when it needs to be moved, and when it does not need to be moved, the base can be stably placed on the ground for use, which will not affect the stability of the device during normal use, thereby improving the applicability of the device.

[0004] Patent No. CN201910670083.8 discloses an environmentally friendly treatment device and method for cosmetic production waste, including a support frame, a storage barrel, a crushing box and a separation box, the storage barrel is arranged on the right side of the support frame, the top of the support frame is fixedly connected to the bottom of the separation box, the middle of the top of the separation box is fixedly connected with a conveying box, the left side of the bottom of the conveying box is connected to the top of the separation box, the right side of the top of the conveying box is fixedly connected to the bottom of the crushing box, and the right side of the top of the conveying box is connected to the bottom of the crushing box. The present invention relates to the technical field of cosmetic processing equipment. The environmentally friendly treatment device and method for cosmetic production waste integrates the sewage treatment system and the glass crushing device, which can not only reduce the consumption of water resources, but also save the expenditure of the enterprise. At the same time, the three-dimensional setting is adopted to save more space, make the utilization of resources more reasonable, and can also break up large condensates in the sewage to facilitate the treatment of sewage.

[0005] In order to ensure the quality of their products and prevent the used cosmetics bottles from being used by unscrupulous merchants, cosmetics manufacturers now need to recycle and crush them. Since there are often residual cosmetics attached to the inside of the bottles, they need to be further cleaned, which not only increases the consumption of water resources, but also increases the production costs of the companies. In addition, when unloading the broken waste bottle fragments, it is easy to affect the collection of the fragments, which makes it inconvenient to unload while collecting, resulting in low collection efficiency.

[0006] During the incineration process of discarded cosmetics, some toxic substances may be emitted, mainly including heavy metals such as lead, mercury, and cadmium: some discarded cosmetics may contain these heavy metals, which will be released when burned, polluting the surrounding environment and causing health hazards.

[0007] The above will cause environmental pollution. In addition, the addition of waste cosmetics may also affect the production efficiency and product quality of cement kilns. Summary of the invention

[0008] 1. Technical issues to be resolved

[0009] In view of the deficiencies in the prior art, the present invention provides a method for the coordinated disposal of waste cosmetics in a cement kiln, which reduces the generation of toxic gases during the incineration process and solves the technical problems of high resource consumption and difficulty in the recycling and treatment of waste cosmetics.

[0010] (II) Technical solution

[0011] To achieve the above objectives, the present invention is implemented through the following technical solutions:

[0012] A method for co-disposing waste cosmetics in a cement kiln, the operating steps of which are as follows:

[0013] The discarded cosmetics are conveyed into a shearing crusher, crushed to 80-100 mm, and then into a drum screen. The screened material enters a pulping tank to obtain material (a); the screened material enters a circulating shearing crusher, and after circulating crushing, it is conveyed into a cement kiln decomposition furnace for incineration; a metal solidifying dispersant is added to the material (a), and the mixture is fully stirred for 10-30 minutes, and the mixture is statically layered. The glass beads are at the top of the liquid and are scooped out using a screen for recycling. The remaining part is then pumped into a sludge tank, the sludge tank slide is opened, and after continuous operation for a certain period of time, the remaining part is conveyed into a cement kiln mixer, mixed and stirred in the mixer, and then conveyed to a plunger pump, which is pumped to the top of the cement kiln decomposition furnace for incineration and disposal. The slag produced by the incineration is mixed into the cement raw meal, and calcined in a rotary kiln to obtain cement clinker.

[0014] In the above technical solution, the specific drum screen is a 5mm drum screen.

[0015] In the above technical solution, the above-screen material is specifically cyclically sheared and crushed to less than 30 mm.

[0016] In the above technical solution, the specific addition amount of the metal solidification dispersant is 1-3%.

[0017] In the above technical solution, the specific preparation method of the metal curing dispersant is:

[0018] S1: Add 100-160 parts of hollow glass microspheres, 500-1000 parts of water, and 3-7 parts of acryl silane coupling agent into a reaction kettle according to weight proportions, stir at 70-80° C. for 100-200 min, filter, and dry to obtain acryl hollow glass microspheres;

[0019] S2: 20-30 parts of pentaerythritol tetrakis (3-mercaptopropionate), 300-400 parts of propylene glycol, 100-200 parts of propylene hollow glass microspheres, 0.002-0.05 parts of tetramercaptoporphyrin, and 2-6 parts of sodium ethoxide are stirred at 70-80° C. for 30-100 minutes to obtain the above-mentioned metal curing dispersant: hollow glass microsphere medium-immobilized 3-mercaptopropionate.

[0020] In the above technical solution, the specific acryl silane coupling agent is selected from one of KH-570 silane coupling agent and γ-methacryloxypropyltrimethoxysilane.

[0021] In the above technical solution, the material (a) is pumped into the sludge pool at a ratio of 20-30%.

[0022] In the above technical solution, the specific continuous operation time of the sludge tank slide is 50 to 60 minutes.

[0023] In the above technical solution, the specific mixing and stirring time in the mixer is 10 to 15 minutes.

[0024] In the above technical solution, the specific calcination temperature of the rotary kiln is 1200-1400°C.

[0025] Reaction mechanism:

[0026] The pentaerythritol tetrakis (3-mercaptopropionate), the propylene hollow glass microspheres, and the tetramercaptoporphyrin undergo a mercapto addition reaction to obtain a metal ligand, which can adsorb metal ions and solidify them on the hollow glass microspheres. At the same time, glycerol disperses the cosmetic residue and dilutes the metal ions therein to facilitate the absorption of the curing agent.

[0027] (III) Beneficial effects

[0028] 1. Most of the discarded cosmetic packaging contains heavy metals, and general treatment will cause pollution. However, this method can effectively utilize the discarded cosmetic packaging, reduce pollution to the environment, and at the same time improve the production efficiency of cement kilns and the quality of cement products. In addition, since cement production is a process with high energy consumption, the use of discarded cosmetics for calorific value recovery is also beneficial to energy conservation.

[0029] 2. Increase the fluidity of waste cosmetics: Mixing waste cosmetics with propylene glycol can increase the fluidity of waste cosmetics, making them easier to flow and mix during the cement production process, thereby improving cement production efficiency and the quality of cement products.

[0030] 3. Suppress the odor of discarded cosmetics: Discarded cosmetics may contain some decomposition products that produce unpleasant odors. Glycerol can inhibit the volatilization of certain components in discarded cosmetics, thereby reducing the generation of odors.

[0031] 4. During the incineration of discarded cosmetics, some toxic substances will be emitted, mainly including heavy metals such as lead, mercury, and cadmium. The present invention is conducive to the glass microbeads to chelate, solidify, and absorb the heavy metals and then take the heavy metals out of the system, thereby avoiding the emission of toxic substances. DETAILED DESCRIPTION

[0032] The technical solution of the present invention will be clearly and completely described below in conjunction with specific implementation methods. Obviously, the described embodiments are only part of the embodiments of the present invention, rather than all of the embodiments. The following description of at least one exemplary embodiment is actually only illustrative and is by no means intended to limit the present invention and its application or use. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0033] Example 1

[0034] A method for co-disposing waste cosmetics in a cement kiln, the operating steps of which are as follows:

[0035] The discarded cosmetics are conveyed into a shear crusher, crushed to about 80 mm, and then into a drum screen. The screened material enters a pulping tank to obtain material (a); the screened material enters a circulating shear crusher, and after circulating crushing, it is conveyed into a cement kiln decomposition furnace for incineration; a metal solidifying dispersant is added to the material (a), and the mixture is fully stirred for 10 minutes, and the mixture is allowed to stand for stratification. The glass beads are at the top of the liquid and are scooped out using a screen for recycling. The remaining part is then pumped into a sludge tank, the sludge tank slide is opened, and after continuous operation for a certain period of time, the remaining part is conveyed into a cement kiln mixer, mixed in the mixer, conveyed to a plunger pump, and pumped to the top of the cement kiln decomposition furnace for incineration and disposal. The slag produced by the incineration is mixed into the cement raw meal, and calcined in a rotary kiln to obtain cement clinker.

[0036] The drum screen is a 5 mm drum screen.

[0037] The material on the screen is cyclically sheared and crushed to less than 30 mm.

[0038] The added amount of the metal solidification dispersant is 1%.

[0039] The preparation method of the metal curing dispersant is:

[0040] S1: 1000 g of hollow glass microspheres, 5000 g of water, and 30 g of acryl silane coupling agent were added into a reaction kettle, stirred at 70° C. for 100 min, filtered, and dried to obtain acryl hollow glass microspheres;

[0041] S2: 200 g of pentaerythritol tetrakis (3-mercaptopropionate), 3000 g of propylene glycol, 1000 g of propylene hollow glass microspheres, 0.1 g of tetramercaptoporphyrin, and 20 g of sodium ethoxide were stirred at 70° C. for 30 minutes to obtain the above-mentioned metal curing dispersant: hollow glass microsphere medium-immobilized 3-mercaptopropionate.

[0042] The acrylic silane coupling agent is selected from KH-570 silane coupling agent.

[0043] The material (a) is pumped into the sludge tank at a ratio of 20%.

[0044] The sludge tank slide has a continuous operation time of 50 minutes.

[0045] The mixing and stirring time in the mixer is 10 minutes.

[0046] The calcining temperature of the rotary kiln is 1200°C.

[0047] Example 2

[0048] A method for co-disposing waste cosmetics in a cement kiln, the operating steps of which are as follows:

[0049] The discarded cosmetics are conveyed into a shear crusher, crushed to 90 mm, and then into a drum screen. The screened material enters a pulping tank to obtain material (a); the screened material enters a circulating shear crusher, and after circulating crushing, it is conveyed into a cement kiln decomposition furnace for incineration; a metal solidifying dispersant is added to the material (a), and the mixture is fully stirred for 20 minutes, and the mixture is allowed to stand for stratification. The glass beads are at the top of the liquid and are scooped out using a screen for recycling. The remaining part is then pumped into a sludge tank, the sludge tank slide is opened, and after continuous operation for a certain period of time, the remaining part is conveyed into a cement kiln mixer, mixed in the mixer, conveyed to a plunger pump, and pumped to the top of the cement kiln decomposition furnace for incineration and disposal. The slag produced by the incineration is mixed into the cement raw meal, and calcined in a rotary kiln to obtain cement clinker.

[0050] The drum screen is a 5 mm drum screen.

[0051] The material on the screen is cyclically sheared and crushed to less than 30 mm.

[0052] The added amount of the metal solidifying dispersant is 2%.

[0053] The preparation method of the metal curing dispersant is:

[0054] S1: 1300 g of hollow glass microspheres, 8000 g of water, and 45 g of acryl silane coupling agent were added into a reaction kettle, stirred at 75° C. for 150 min, filtered, and dried to obtain acryl hollow glass microspheres;

[0055] S2: 250 g of pentaerythritol tetrakis (3-mercaptopropionate), 3500 g of propylene glycol, 1500 g of propylene hollow glass microspheres, 0.25 g of tetramercaptoporphyrin, and 40 g of sodium ethoxide were stirred at 75° C. for 70 minutes to obtain the above-mentioned metal curing dispersant: hollow glass microsphere medium-immobilized 3-mercaptopropionate.

[0056] The acrylic silane coupling agent is selected from KH-570 silane coupling agent.

[0057] The material (a) is pumped into the sludge tank at a ratio of 25%.

[0058] The sludge tank slide has a continuous operation time of 55 minutes.

[0059] The mixing and stirring time in the mixer is 12 minutes.

[0060] The calcining temperature of the rotary kiln is 1300°C.

[0061] Example 3

[0062] A method for co-disposing waste cosmetics in a cement kiln, the operating steps of which are as follows:

[0063] The discarded cosmetics are conveyed into a shear crusher, crushed to 100 mm, and then into a drum screen. The screened material enters a pulping tank to obtain material (a); the screened material enters a circulating shear crusher, and after circulating crushing, it is conveyed into a cement kiln decomposition furnace for incineration; a metal solidifying dispersant is added to the material (a), and the mixture is fully stirred for 30 minutes, and allowed to stand for stratification. The glass beads are at the top of the liquid and are scooped out using a screen for recycling. The remaining part is then pumped into a sludge tank, the sludge tank slide is opened, and after continuous operation for a certain period of time, it is conveyed into a cement kiln mixer, mixed and stirred in the mixer for 15 minutes, conveyed to a plunger pump, and pumped to the top of the cement kiln decomposition furnace for incineration and disposal. The slag produced by the incineration is mixed into the cement raw meal, and calcined in a rotary kiln to obtain cement clinker.

[0064] The drum screen is a 5 mm drum screen.

[0065] The material on the screen is cyclically sheared and crushed to less than 30 mm.

[0066] The added amount of the metal solidifying dispersant is 3%.

[0067] The preparation method of the metal curing dispersant is:

[0068] S1: 1600 g of hollow glass microspheres, 10000 g of water, and 70 g of acryl silane coupling agent were added into a reaction kettle, stirred at 80° C. for 200 min, filtered, and dried to obtain acryl hollow glass microspheres;

[0069] S2: 300 g of pentaerythritol tetrakis (3-mercaptopropionate), 4000 g of propylene glycol, 2000 g of propylene hollow glass microspheres, 0.5 g of tetramercaptoporphyrin, and 60 g of sodium ethoxide were stirred at 80° C. for 100 minutes to obtain the above-mentioned metal curing dispersant: hollow glass microsphere medium-immobilized 3-mercaptopropionate.

[0070] The acryl silane coupling agent is selected from γ-methacryloxypropyltrimethoxysilane.

[0071] The material (a) is pumped into the sludge tank at a ratio of 30%.

[0072] The sludge tank slide has a continuous operation time of 60 minutes.

[0073] The mixing and stirring time in the mixer is 15 minutes.

[0074] The calcining temperature of the rotary kiln is 1400°C.

[0075] Comparative Example 1

[0076] A method for co-disposing waste cosmetics in a cement kiln, the operating steps of which are as follows:

[0077] The discarded cosmetics are conveyed into a shearing crusher, crushed to about 80 mm, and then enter a drum screen. The screened material enters a pulping tank to obtain material (a); the screened material enters a circulating shearing crusher, and after circulating crushing, it is sent to a cement kiln decomposition furnace for incineration; propylene glycol is added to the material (a), and the mixture is fully stirred for 10 minutes, and the mixture is allowed to stand for stratification. The glass beads are at the top of the liquid and are scooped out using a wire mesh for recycling. The remaining part is then pumped into a sludge tank, the sludge tank slide is opened, and after continuous operation for a certain period of time, it is sent to a cement kiln mixer, mixed in the mixer, and then conveyed to a plunger pump, which is pumped to the top of the cement kiln decomposition furnace for incineration and disposal. The slag produced by the incineration is mixed into cement raw materials, and calcined in a rotary kiln to obtain cement clinker.

[0078] The drum screen is a 5 mm drum screen.

[0079] The material on the screen is cyclically sheared and crushed to less than 30 mm.

[0080] The added amount of glycerol is 1%.

[0081] The material (a) is pumped into the sludge tank at a ratio of 20%.

[0082] The sludge tank slide has a continuous operation time of 50 minutes.

[0083] The mixing and stirring time in the mixer is 10 minutes.

[0084] The calcining temperature of the rotary kiln is 1200°C.

[0085] Comparative Example 2

[0086] A method for co-disposing waste cosmetics in a cement kiln, the operating steps of which are as follows:

[0087] The discarded cosmetics are conveyed into a shear crusher, crushed to about 80 mm, and then into a drum screen. The screened material enters a pulping tank to obtain material (a); the screened material enters a circulating shear crusher, and after circulating crushing, it is conveyed into a cement kiln decomposition furnace for incineration; a metal solidifying dispersant is added to the material (a), and the mixture is fully stirred for 10 minutes, and the mixture is allowed to stand for stratification. The glass beads are at the top of the liquid and are scooped out using a screen for recycling. The remaining part is then pumped into a sludge tank, the sludge tank slide is opened, and after continuous operation for a certain period of time, the remaining part is conveyed into a cement kiln mixer, mixed in the mixer, conveyed to a plunger pump, and pumped to the top of the cement kiln decomposition furnace for incineration and disposal. The slag produced by the incineration is mixed into the cement raw meal, and calcined in a rotary kiln to obtain cement clinker.

[0088] The drum screen is a 5 mm drum screen.

[0089] The material on the screen is cyclically sheared and crushed to less than 30 mm.

[0090] The added amount of the metal solidification dispersant is 1%.

[0091] The preparation method of the metal curing dispersant is:

[0092] S1: 1000 g of hollow glass microspheres, 5000 g of water, and 30 g of acryl silane coupling agent were added into a reaction kettle, stirred at 70° C. for 100 min, filtered, and dried to obtain acryl hollow glass microspheres;

[0093] S2: 200 g of pentaerythritol tetrakis (3-mercaptopropionate), 3000 g of propylene glycol, 1000 g of propylene hollow glass microspheres, and 20 g of sodium ethoxide were stirred at 70° C. for 30 minutes to obtain the above-mentioned metal curing dispersant: hollow glass microsphere medium-immobilized 3-mercaptopropionate.

[0094] The acrylic silane coupling agent is selected from KH-570 silane coupling agent.

[0095] The material (a) is pumped into the sludge tank at a ratio of 20%.

[0096] The sludge tank slide has a continuous operation time of 50 minutes.

[0097] The mixing and stirring time in the mixer is 10 minutes.

[0098] The calcining temperature of the rotary kiln is 1200°C.

[0099] Comparative Example 3

[0100] A method for co-disposing waste cosmetics in a cement kiln, the operating steps of which are as follows:

[0101] The discarded cosmetics are conveyed into a shear crusher, crushed to about 80 mm, and then into a drum screen. The screened material enters a pulping tank to obtain material (a); the screened material enters a circulating shear crusher, and after circulating crushing, it is conveyed into a cement kiln decomposition furnace for incineration; a metal solidifying dispersant is added to the material (a), and the mixture is fully stirred for 10 minutes, and the mixture is allowed to stand for stratification. The glass beads are at the top of the liquid and are scooped out using a screen for recycling. The remaining part is then pumped into a sludge tank, the sludge tank slide is opened, and after continuous operation for a certain period of time, the remaining part is conveyed into a cement kiln mixer, mixed in the mixer, conveyed to a plunger pump, and pumped to the top of the cement kiln decomposition furnace for incineration and disposal. The slag produced by the incineration is mixed into the cement raw meal, and calcined in a rotary kiln to obtain cement clinker.

[0102] The drum screen is a 5 mm drum screen.

[0103] The material on the screen is cyclically sheared and crushed to less than 30 mm.

[0104] The added amount of the metal solidification dispersant is 1%.

[0105] The preparation method of the metal curing dispersant is:

[0106] S1: 1000 g of hollow glass microspheres, 5000 g of water, and 30 g of acryl silane coupling agent were added into a reaction kettle, stirred at 70° C. for 100 min, filtered, and dried to obtain acryl hollow glass microspheres;

[0107] S2: 3000 g of propylene glycol, 1000 g of propylene hollow glass microspheres, 0.1 g of tetramercaptoporphyrin, and 20 g of sodium ethoxide were stirred at 70° C. for 30 minutes to obtain the above-mentioned metal solidification dispersant: hollow glass microsphere medium-immobilized 3-mercaptopropionate.

[0108] The acrylic silane coupling agent is selected from KH-570 silane coupling agent.

[0109] The material (a) is pumped into the sludge tank at a ratio of 20%.

[0110] The sludge tank slide has a continuous operation time of 50 minutes.

[0111] The mixing and stirring time in the mixer is 10 minutes.

[0112] The calcining temperature of the rotary kiln is 1200°C.

[0113] The slag after incineration in the above examples and comparative examples was subjected to toxicity leaching test according to the national standard (HJ557-2010). The toxicity leaching results are shown in Table 1 below:

[0114] Table 1 Heavy metal leaching concentration data table

[0115]

[0116] The technical features of the above-described embodiments may be arbitrarily combined. To make the description concise, not all possible combinations of the technical features in the above-described embodiments are described. However, as long as there is no contradiction in the combination of these technical features, they should be considered to be within the scope of this specification.

[0117] The above-mentioned embodiments only express several implementation methods of the present invention, and the descriptions thereof are relatively specific and detailed, but they cannot be understood as limiting the scope of the invention patent. It should be pointed out that, for ordinary technicians in this field, several variations and improvements can be made without departing from the concept of the present invention, and these all belong to the protection scope of the present invention. Therefore, the protection scope of the patent of the present invention shall be subject to the attached claims.

Claims

1. A method for co-disposal of waste cosmetics in a cement kiln, the operating steps of which are: The discarded cosmetics are conveyed into a shear crusher, crushed to 80-100 mm, and then into a drum screen. The screened material enters a pulping tank to obtain material (a); the screened material enters a circulating shear crusher, and after circulating crushing, it is sent to a cement kiln decomposition furnace for incineration; a metal solidifying dispersant is added to the material (a), and the mixture is fully stirred for 10-30 minutes, and the mixture is allowed to stand for stratification. The glass beads are at the top of the liquid and are scooped out using a screen for recycling. The remaining part is then pumped into a sludge tank, the sludge tank slide is opened, and after continuous operation for a certain period of time, the remaining part is sent into a cement kiln mixer, mixed and stirred in the mixer, and then conveyed to a plunger pump, which is pumped to the top of the cement kiln decomposition furnace for incineration and disposal. The slag produced by the incineration is mixed into the cement raw meal, and calcined in a rotary kiln to obtain cement clinker; The preparation method of the metal curing dispersant is: S1: Add 100-160 parts of hollow glass microspheres, 500-1000 parts of water, and 3-7 parts of acryl silane coupling agent into a reaction kettle according to weight proportions, stir at 70-80° C. for 100-200 min, filter, and dry to obtain acryl hollow glass microspheres; S2: According to the mass proportions, 20-30 parts of pentaerythritol tetrakis (3-mercaptopropionate), 300-400 parts of propylene glycol, 100-200 parts of propylene hollow glass microspheres, 0.002-0.05 parts of tetramercaptoporphyrin, and 2-6 parts of sodium ethoxide are stirred at 70-80° C. for 30-100 minutes to obtain the above-mentioned metal curing dispersant.

2. The method for co-disposal of waste cosmetics by cement kiln according to claim 1, Features: The drum screen is a 5 mm drum screen.

3. The method for co-disposal of waste cosmetics by cement kiln according to claim 1, Features: The material on the screen is cyclically sheared and crushed to less than 30 mm.

4. The method for co-disposal of waste cosmetics by cement kiln according to claim 1, Features: The metal curing dispersant is added in an amount of 1-3%.

5. The method for co-disposal of waste cosmetics by cement kiln according to claim 1, Features: The acrylic silane coupling agent is selected from KH-570 silane coupling agent.

6. The method for co-disposal of waste cosmetics by cement kiln according to claim 1, Features: The material (a) is pumped into the sludge tank at a ratio of 20-30%.

7. The method for co-disposal of waste cosmetics by cement kiln according to claim 1, Features: The sludge tank slide can run continuously for 50-60 minutes.

8. The method for co-disposal of waste cosmetics by cement kiln according to claim 1, Features: The mixing time in the mixer is 10-15 minutes.

9. The method for co-disposal of waste cosmetics by cement kiln according to claim 1, Features: The calcination temperature of the rotary kiln is 1200-1400℃.

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