CN201241099Y - Novel environment protection waste old rubber plastic extractive decomposing fractionator - Google Patents
Novel environment protection waste old rubber plastic extractive decomposing fractionator Download PDFInfo
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- CN201241099Y CN201241099Y CNU2008201477855U CN200820147785U CN201241099Y CN 201241099 Y CN201241099 Y CN 201241099Y CN U2008201477855 U CNU2008201477855 U CN U2008201477855U CN 200820147785 U CN200820147785 U CN 200820147785U CN 201241099 Y CN201241099 Y CN 201241099Y
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- hydrocarbon fuel
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- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
The utility model discloses a novel Environment-friendly waste rubber plastic refined decomposition fractionator, which mainly comprises a refined decomposition kettle body, a fractionating tower arranged at the upper part of the refined decomposition kettle body, a light hydrocarbon fuel condenser and a heavy hydrocarbon fuel condenser connected with the fractionating tower, and a light hydrocarbon fuel product storage tank and a heavy hydrocarbon fuel product storage tank connected with the light hydrocarbon fuel condenser and the heavy hydrocarbon fuel condenser, wherein, a light hydrocarbon fractionating chamber, a heavy hydrocarbon fractionating chamber and a catalyst chamber are disposed in the fractionating tower. A stainless steel net catalyst bed is arranged in the fractionating tower. A connecting flange is arranged at the joint part of the refined decomposition kettle body and the fractionating tower. A temperature control device is disposed on the side face of the refined decomposition kettle body. Three chambers are arranged in the fractionating tower, the fineness of separation and cracking of hydrocarbon products can be improved, and the capacity utilization rate can be greatly improved, the pollution to the environment by waste rubber plastics can be eliminated, new energy sources can also be added, the purposes of recycling resources and changing waste into valuables can be achieved, the product cost is low, and the economic benefit is good.
Description
Technical field:
The utility model relates to a kind of chemical industry equipment, relates in particular to a kind of oil fuel that waste old or plastic prod are carried out producing after the thermo-cracking and carries out the isolating novel environment friendly waste and old rubber of hydrocarbon products essence and separate fractionator.
Background technology:
Along with industry, expanding economy, rubber, raw materials for plastics production usage quantity are increasing, and all trades and professions all be unable to do without rubber, plastic prod, and the waste and old rubbish that brings thus causes environmental pollution also to be on the rise.For example plastic shopping bag is the easily-consumed products in the daily life, and China all will consume a large amount of plastic shopping bags every year.Plastic shopping bag uses and recycles reasons such as not in place owing to excessive when facilitating for the human consumer, also caused the serious energy, the wasting of resources and environmental pollution.Particularly the super-thin plastic shopping bag is damaged easily, is arbitrarily abandoned mostly, becomes the main source of " white pollution ".Producing, selling and uying of plastic shopping bag limited in more and more countries and area at present.For implementing a scientific outlook on development; build a resource-conserving society and friendly environment society; take effective measures from the source; supervise enterprise to produce plastic shopping bag durable, that be easy to reclaim; guiding, the encouragement masses rationally use plastic shopping bag, promote comprehensive utilization of resources, preserve the ecological environment; further advance energy-saving and emission-reduction work, China General Office of the State Council issued notice about limit production, sale, use plastic shopping bag on December 31st, 2007.
Therefore, solve the plastic refuse pollution on the environment, simultaneously plastic refuse being recycled is a very important problem, at present, there is report to begin the waste and old rubber product is handled, up to the present, people have proposed the various methods that plastic refuse is handled.Generally be to adopt catalyzer that plastic refuse is carried out catalysis and thermo-cracking.For example USP4851401 discloses a kind of method of disposal of plastic waste, comprise and earlier plastic refuse being pulverized, thermally splitting takes place in cracking still, and catalytic cracking takes place in gas products again under catalyst action, and then adopts conventional technology that the product that obtains is separated.But have following shortcoming: treatment capacity is little, is difficult to form scale and benefit.And this processing only is bulk processing, and organism is in cracking process, and it is second-rate to handle products obtained therefrom, and economic benefit is relatively low.
The utility model content:
In order to reduce the waste and old rubber pollution on the environment, and this kind nuisance become help society and the common people's product, it is second-rate to handle products obtained therefrom when solution has waste and old rubber product treatment device processes now, the shortcoming that economic benefit is relatively low, the purpose of this utility model provide a kind ofly can carry out the isolating novel environment friendly waste and old rubber of hydrocarbon products essence to the oil fuel that waste old or rubber and plastic product carry out producing after the thermo-cracking and separate fractionator.
The technical solution of the utility model realizes with following method:
A kind of novel environment friendly waste and old rubber essence is separated fractionator, comprise that mainly essence separates kettle 4, be arranged on essence and separate the separation column 1 on kettle 4 tops, light hydrocarbon fuel condenser 13 that is connected with separation column 1 and heavy hydrocarbon fuel condenser 14, the light hydrocarbon fuel product hold-up vessel 16 and the heavy hydrocarbon fuel product hold-up vessel 17 that are connected with heavy hydrocarbon fuel condenser 14 with light hydrocarbon fuel condenser 13, wherein, described separation column 1 inside is provided with light hydrocarbon fractionation chamber 19, heavy hydrocarbon fractionation chamber 20 and catalyst chamber 21.
The light hydrocarbon fractionation chamber 19 of separation column 1 inside, heavy hydrocarbon fractionation chamber 20 are provided with catalytic bed 25 with catalyst chamber 21.
Described catalytic bed 25 is a stainless (steel) wire.
Described essence is separated kettle 4 and separation column 1 joint and is provided with to be connected and sends out blue 2.
Described essence is separated kettle 4 sides and is provided with temperature measuring equipment 12.
Positively effect of the present utility model is:
Separation column of the present utility model inside is provided with three chambers, improved the fineness of hydrocarbon products separating and cracking, and the production capacity rate improves greatly, both eliminated of the pollution of waste rubber plastics to environment, increased the new energy again, reached resource circulation utilization, the purpose that turns waste into wealth, product cost is low, good in economic efficiency.
Description of drawings:
Fig. 1 separates the fractionator structural representation for the utility model essence.
Fig. 2 is a separation column structural representation of the present utility model.
Embodiment:
Below in conjunction with accompanying drawing and embodiment the technical solution of the utility model is further described:
As seen from Figure 1, this novel environment friendly waste and old rubber essence is separated fractionator, comprise that mainly essence separates kettle 4, be arranged on essence and separate the discharge port 5 of kettle 4 bottoms, be arranged on essence and separate the separation column 1 on kettle 4 tops, separation column 1 is divided into three chambers, from top to bottom, the superiors are gasoline fractionation chamber 19, the inferior upper strata oil content of attaching most importance to heats up in a steamer chamber 20, lower floor is a catalyst chamber 21, gasoline fractionation chamber 19 outer additive inlet 6 and the additive outlets 7 of being provided with, heavy oil fractionation chamber 20 outer additive inlet 8 and the additive outlets 9 of being provided with, catalyst chamber 21 outer additive inlet 10 and the additive outlets 11 of being provided with, the gasoline fractionation chamber 19 outer fuel dispensing outlets 22 that also are provided with, fuel dispensing outlet 22 is connected with gasoline condenser 13, and heavy oil fractionation chamber 20 is outside equipped with heavy oil outlet 23, and heavy oil outlet 23 is connected with heavy oil condenser 14, gasoline condenser 13 is connected with gasoline products hold-up vessel 16, and heavy oil condenser 14 is connected with heavy oil product hold-up vessel 17.Separate in essence on the discharge port 5 of kettle thermocouple thermometer 12 is housed.Separation column 1 bottom is provided with smart and separates the connection that kettle 4 is connected and send out orchid 2.
By Fig. 1 and Fig. 2 as can be seen, separating on the kettle 4 side in essence is provided with the opening for feed 3, the essence that are communicated with oil pump and separates the reaction kettle body thermometer is housed in the kettle 4, in the gasoline fractionation chamber 19 of separation column gasoline fractionation chamber thermopair 24 is housed, heavy oil fractionation chamber thermopair 26 is equipped with in heavy oil fractionation chamber 20, is communicated with gasoline delivery valve 15 with gasoline condenser 13; Be communicated with heavy oil delivery valve 18 with heavy oil condenser 14.
As seen from Figure 2, separation column 1 is to be divided into three layers of vertical separation column with stainless (steel) wire, and separation column 1 periphery is surrounded by thermal insulation layer 28, on every layer of fractionation chamber interior walls the back flow plate 27 that is the inclined-plane is housed.
Claims (5)
1, a kind of novel environment friendly waste and old rubber essence is separated fractionator, comprise that mainly essence separates kettle (4), be arranged on essence and separate the separation column (1) on kettle (4) top, light hydrocarbon fuel condenser (13) that is connected with separation column (1) and heavy hydrocarbon fuel condenser (14), light hydrocarbon fuel product hold-up vessel (16) and heavy hydrocarbon fuel product hold-up vessel (17) with light hydrocarbon fuel condenser (13) is connected with heavy hydrocarbon fuel condenser (14) is characterized in that: described separation column (1) inside is provided with light hydrocarbon fractionation chamber (19), heavy hydrocarbon fractionation chamber (20) and catalyst chamber (21).
2, novel environment friendly waste and old rubber essence according to claim 1 is separated fractionator, it is characterized in that: inner light hydrocarbon fractionation chamber (19), the heavy hydrocarbon fractionation chamber (20) of separation column (1) is provided with catalytic bed (24) with catalyst chamber (21).
3, novel environment friendly waste and old rubber essence according to claim 2 is separated fractionator, it is characterized in that: described catalytic bed (24) is a stainless (steel) wire.
4, novel environment friendly waste and old rubber essence according to claim 1 is separated fractionator, it is characterized in that: described essence is separated kettle (4) and separation column (1) joint and is provided with to be connected and sends out blue (2).
5, novel environment friendly waste and old rubber essence according to claim 1 is separated fractionator, it is characterized in that: described essence is separated kettle (4) side and is provided with temperature measuring equipment (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201477855U CN201241099Y (en) | 2008-07-02 | 2008-07-02 | Novel environment protection waste old rubber plastic extractive decomposing fractionator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201477855U CN201241099Y (en) | 2008-07-02 | 2008-07-02 | Novel environment protection waste old rubber plastic extractive decomposing fractionator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201241099Y true CN201241099Y (en) | 2009-05-20 |
Family
ID=40714393
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008201477855U Expired - Fee Related CN201241099Y (en) | 2008-07-02 | 2008-07-02 | Novel environment protection waste old rubber plastic extractive decomposing fractionator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201241099Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105016987A (en) * | 2015-07-09 | 2015-11-04 | 任广鸿 | Method and device for recycling industrial waste containing nylon 66 triglycol |
| CN105131270A (en) * | 2015-08-19 | 2015-12-09 | 上海联景高分子材料有限公司 | Fractionators narrowing polyester polyol molecular weight distribution |
-
2008
- 2008-07-02 CN CNU2008201477855U patent/CN201241099Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105016987A (en) * | 2015-07-09 | 2015-11-04 | 任广鸿 | Method and device for recycling industrial waste containing nylon 66 triglycol |
| CN105131270A (en) * | 2015-08-19 | 2015-12-09 | 上海联景高分子材料有限公司 | Fractionators narrowing polyester polyol molecular weight distribution |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090520 Termination date: 20120702 |