阅读说明：本技术 微晶蜡生产工艺 (Microcrystalline wax production process ) 是由 陈晓敏 于 2019-10-16 设计创作，主要内容包括：一种微晶蜡生产工艺,包括溶化罐、保温罐、喷头、收集管、传输带和装卸斗,所述溶化罐上设有用于进蜡的第一进料口,溶化罐上设有进高温水的进水口,溶化罐上设有用于出蜡液的第一出料口,第一出料口上设有第一管道,第一管道上设有第一泵,所述保温罐上设有第二进料口,第二进料口与第一管道相通,保温罐上设有第二出料口,第二出料口上设有第二管道,第二管道上设有第二泵,第二管道向上方延伸一定高度,第二管道末端设有喷头,喷头下方设有收集罐,收集罐下方设有传输带,传输带末端设有装卸斗。该微晶蜡生产工艺工艺简单,而且结构紧凑,设备成本和生产成本低,通过高空喷粒和冷却形成比较规整的1.2mm的高度微晶蜡。(The utility model provides a microcrystalline wax production technology, is including dissolving jar, holding tank, shower nozzle, collecting pipe, transmission band and loading and unloading fill, dissolving the first feed inlet that is equipped with on the jar and is used for into wax, dissolving the water inlet that is equipped with into high-temperature water on the jar, dissolving the first discharge gate that is equipped with on the jar and is used for going out wax liquid, being equipped with first pipeline on the first discharge gate, being equipped with first pump on the first pipeline, be equipped with the second feed inlet on the holding tank, second feed inlet and first pipeline communicate with each other, are equipped with the second discharge gate on the holding tank, are equipped with the second pipeline on the second discharge gate, are equipped with the second pump on the second pipeline, and the second pipeline upwards extends a take the altitude, and the second pipeline end is equipped with the shower nozzle, and the shower. The microcrystalline wax has the advantages of simple production process, compact structure, low equipment cost and production cost, and regular 1.2mm high microcrystalline wax is formed by high-altitude grain spraying and cooling.)

1. The utility model provides a microcrystalline wax production technology, its characterized in that, is including dissolving jar, heat preservation jar, shower nozzle, collecting pipe, transmission band and loading and unloading fill, dissolving and being equipped with the first feed inlet that is used for into wax on the jar, dissolving the water inlet that is equipped with into high-temperature water on the jar, dissolving and being equipped with the first discharge gate that is used for going out the wax liquid on the jar, be equipped with first pipeline on the first discharge gate, be equipped with first pump on the first pipeline, be equipped with the second feed inlet on the heat preservation jar, the second feed inlet communicates with each other with first pipeline, is equipped with the second discharge gate on the heat preservation jar, is equipped with the second pipeline on the second discharge gate, is equipped with the second pump on the second pipeline, and the second pipeline extends the take the altitude to the top, and the second pipeline end is equipped.

2. The microcrystalline wax production process according to claim 1, wherein a conical collection hopper is arranged at the bottom end of the collection tank, and a third discharge hole is formed in the bottom of the collection hopper.

3. A microcrystalline wax producing process according to any of claims 1-2, characterised in that a sub-packaging bag is arranged below the loading and unloading hopper.

Technical Field

The invention relates to a wax production process, in particular to a microcrystalline wax production process.

Background

With the development and change of the machinery industry and the use of novel engines and the requirements of energy conservation and environmental protection, the quality requirement of the microcrystalline wax is higher and higher, and the medium-high grade microcrystalline wax with excellent physical and chemical properties in the market, especially the high grade microcrystalline wax, is increasingly favored by people. The existing high-degree microcrystalline wax production process is complex, high in cost and not energy-saving, and the traditional high-degree microcrystalline wax production process cannot obtain regular high-degree microcrystalline wax.

disclosure of Invention

The invention aims to provide a microcrystalline wax production process with simple process and compact structure.

In order to solve the technical problem, the invention provides a microcrystalline wax production process which comprises a melting tank, a heat preservation tank, a spray head, a collecting pipe, a conveying belt and a loading and unloading hopper, wherein a first feed port for feeding wax is formed in the melting tank, a water inlet for feeding high-temperature water is formed in the melting tank, a first discharge port for discharging wax liquid is formed in the melting tank, a first pipeline is arranged on the first discharge port, a first pump is arranged on the first pipeline, a second feed port is formed in the heat preservation tank and communicated with the first pipeline, a second discharge port is formed in the heat preservation tank, a second pipeline is arranged on the second discharge port, a second pump is arranged on the second pipeline, the second pipeline extends upwards to a certain height, the spray head is arranged at the tail end of the second pipeline, the collecting tank is arranged below the spray head, the conveying belt is arranged below.

For better collection 1.2mm high microcrystalline wax, collection tank bottom end is equipped with the toper and collects the fill, collects the fill bottom and is equipped with the third discharge gate.

In order to facilitate the subpackaging of the microcrystalline wax with the height of 1.2mm, a subpackaging bag is arranged below the loading and unloading hopper.

The invention has the beneficial effects that: the microcrystalline wax has the advantages of simple production process, no need of complex processing equipment, compact structure, low equipment cost and production cost, and formation of regular 1.2mm high microcrystalline wax by high-altitude grain spraying and cooling.

Drawings

FIG. 1 is a schematic structural view of a microcrystalline wax production process of the present invention;

Description of reference numerals: 1-a melting tank; 101-a first feed port; 102-a water inlet; 103-a first discharge port; 2-a heat preservation tank; 201-a second feed port; 202-a second discharge hole; 3-a spray head; 4-a collection tank; 401-a collection hopper; 402-a third discharge port; 5, conveying the belt; 6-loading and unloading bucket; 7-a first conduit; 8-a first pump; 9-a second conduit; 10-a second pump; 11-split bagging;

Detailed Description

In order to explain technical contents, structural features, and objects and effects of the present invention in detail, the following detailed description is given with reference to the accompanying drawings in conjunction with the embodiments.

Referring to the attached figure 1, the invention provides a microcrystalline wax production process, which comprises a melting tank 1, a heat-insulating tank 2, a spray head 3, a collection tank 4, a transmission belt 5 and a loading and unloading hopper 6, wherein a first feed port 101 for feeding wax is arranged on the melting tank 1, a water inlet 102 for feeding high-temperature water is arranged on the melting tank 1, a first discharge port 103 for discharging wax liquid is arranged on the melting tank 1, a first pipeline 7 is arranged on the first discharge port 103, a first pump 8 is arranged on the first pipeline 7, a second feed port 201 is arranged on the heat-insulating tank 2, the second feed port 201 is communicated with the first pipeline 7, a second discharge port 202 is arranged on the heat-insulating tank 2, a second pipeline 9 is arranged on the second pipeline 9, a second pump 10 is arranged on the second pipeline 9, the second pipeline 9 extends upwards for a certain height, the spray head 3 is arranged at the tail end of the second pipeline 9, the collection tank 4 is arranged below the, the tail end of the transmission belt 5 is provided with a loading and unloading hopper 6.

In this embodiment, the dissolving tank 1 is a high-pressure tank, the temperature of the high-temperature water in the dissolving tank 1 is above 100 ℃, and the temperature of the high-temperature water is 110-130 ℃.

In this embodiment, the distance between the spray head 3 and the ground is more than 20 meters. After the spray head 3 sprays the wax pellets, the wax pellets are cooled by a stroke of 20m to form microcrystalline wax having a height of 1.2 mm.

In this embodiment, the bottom end of the collecting tank 4 is provided with a conical collecting hopper 401, and the bottom of the collecting hopper 401 is provided with a third discharge hole 402. After the wax particles are sprayed by the spray head 3, the wax particles are cooled to form microcrystalline wax with the height of 1.2mm in the falling process of the collecting tank 4, then fall into the collecting hopper 401, and finally are conveyed onto the conveying belt 5 through the third discharge hole 402.

In this embodiment, a separate packaging bag 11 is provided below the loading and unloading hopper 6. The subpackage bag 11 can subpackage the processed high microcrystalline wax.

when the microcrystalline wax production process works, high-temperature water is firstly injected into the melting tank 1 from the water inlet 102, then, wax is put into the melting tank 1 from the first feeding hole 101, the wax is melted into wax liquid by high-temperature water with the temperature of 110-130 ℃, the wax liquid is precipitated, when the temperature of the wax liquid is reduced to 90-120 ℃, the wax liquid is conveyed into the heat preservation tank 2 through the first pump 8, carry the wax liquid in the holding tank 2 in the second pipeline 9 through second pump 10, the wax liquid prolongs second pipeline 9 and reaches 20m eminence shower nozzle 3, the wax liquid spouts a wax grain through shower nozzle 3, the wax grain cools off through 20m stroke in collection tank 4 and becomes 1.2mm high microcrystalline wax, high microcrystalline wax is carried on transmission band 5 through third discharge gate 402 after being collected by collection fill 401, high microcrystalline wax is the secondary cooling when transmission band 5 conveys, high microcrystalline wax is collected by the terminal loading and unloading fill 6 of transmission band 5 at last and is passed through partial shipment bag 11 partial shipment.

The microcrystalline wax has the advantages of simple production process, no need of complex processing equipment, compact structure, low equipment cost and production cost, and formation of regular 1.2mm high microcrystalline wax by high-altitude grain spraying and cooling.

The above description is only an embodiment of the present invention, and not intended to limit the scope of the present invention, and all modifications of equivalent structures and equivalent processes performed by the present specification and drawings, or directly or indirectly applied to other related technical fields, are included in the scope of the present invention.