CN1093162C - Process for producing vaseline using waste plastics as raw material - Google Patents
Process for producing vaseline using waste plastics as raw material Download PDFInfo
- Publication number
- CN1093162C CN1093162C CN96117443A CN96117443A CN1093162C CN 1093162 C CN1093162 C CN 1093162C CN 96117443 A CN96117443 A CN 96117443A CN 96117443 A CN96117443 A CN 96117443A CN 1093162 C CN1093162 C CN 1093162C
- Authority
- CN
- China
- Prior art keywords
- vaseline
- gas
- waste
- raw material
- liquid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000000034 method Methods 0.000 title claims abstract description 15
- 229940099259 vaseline Drugs 0.000 title claims abstract description 15
- 239000004033 plastic Substances 0.000 title claims abstract description 14
- 229920003023 plastic Polymers 0.000 title claims abstract description 14
- 239000002699 waste material Substances 0.000 title claims abstract description 14
- 239000002994 raw material Substances 0.000 title claims abstract description 10
- 238000005336 cracking Methods 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 9
- 238000004519 manufacturing process Methods 0.000 claims abstract description 9
- 239000003054 catalyst Substances 0.000 claims abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 3
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 3
- 239000004571 lime Substances 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract description 3
- 239000003921 oil Substances 0.000 description 7
- -1 polyethylene Polymers 0.000 description 5
- 239000004743 Polypropylene Substances 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 229920001155 polypropylene Polymers 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 150000001335 aliphatic alkanes Chemical class 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 229920002521 macromolecule Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920001617 Vinyon Polymers 0.000 description 1
- 238000010504 bond cleavage reaction Methods 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000003137 locomotive effect Effects 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Landscapes
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The present invention relates to a method for producing vaseline by using waste and old plastics, which is characterized in that after the waste and old plastics are cleaned, catalyst is added into the plastics to carry out cracking reaction; after gas and liquid which are generated by the cracking process are pumped out by negative pressure, the gas and the liquid are directly filtered to be discolored, and then, the gas and the liquid are cooled to form the vaseline after filtered. The method of the present invention has the advantages of low cost of raw materials, simple technology, low production cost, etc.
Description
The present invention goes on foot and be a kind of is the method for raw material production Vaseline with the waste or used plastics.
At present, Vaseline be by in the process of oil production to pay a product be raw material through refining forming repeatedly.This method is with the product of paying in its process of oil production, the throw out that generates after cooling off such as oil residues after the crude distillation of paraffin wax base; It two is throw outs in the petroleum storage tanks; Three to be locomotive oils handle resistates through solvent recuperation with solvent dewaxed for it; Its four are production premium motor fuel concentrated things of paying product etc. for raw material through heating, remove lower boiling oil, by activated carbon or atlapulgite, removal of impurities, decolouring, deodorizing etc. are refined repeatedly and are formed.This method existence repeats operations such as heating, decolouring, removal of impurities, causes complex process, shortcomings such as energy consumption height.
The objective of the invention is with the waste or used plastics is raw material, produces the method for Vaseline, and it is low that this method has a cost, product yield height, advantage such as technology is simple.
The object of the present invention is achieved like this.Waste or used plastics after handling, is dropped into reactor in cleaning, add ripe, behind the catalyzer such as lime or atlapulgite or activated carbon, the cracking of heating, its cracking temperature is controlled at 320 ℃ to 480 ℃, the gas that institute's cracking generates is extracted reactor out with vacuum, its negative pressure is controlled at 0.04 to 0.12 normal atmosphere, the gas-liquid process that vacuum is extracted out is filtered, after decolouring by the decolorizer that is equipped with catalyzer such as gac or atlapulgite, filter again, promptly make the Vaseline product after the cooling.
Below in conjunction with embodiment the present invention is further described.
After waste or used plastics cleaned, drop into tubular type scission reaction still, add white lime or catalyzer such as atlapulgite or activated carbon, with fiery reacting by heating still, temperature is controlled between 320 ℃ to 480 ℃, make its plastic cracking, take out method with the fast reactor that detaches of splitting gas with vacuum, its negative pressure is controlled between 0.04 to 0.12 normal atmosphere, the gas-liquid of its extraction is directly filtered through filtering net, the decolorizer that the gas-liquid of handling after filtration is transported to gac or atlapulgite carries out filtration treatment by filter cloth after decolouring and handling again, promptly makes the Vaseline product after the cooling; Lower boiling liquid still when gaseous state, is drawn in the pressure-pot and must pays product, solvent oil, detergent use oil.The gas that can not liquefy then in the suction gas tank, must pay product big right gas at normal temperatures.
Its principal reaction is as follows:
1. use the polyethylene waste material:
Number is less than rare hydrocarbon of 24, alkane, and wherein n is a carbonatoms in the macromolecular compound polyethylene, n
1It is 22 to 32 number.
2. use the polypropylene waste material
Atomicity is less than 24 rare hydrocarbon, alkane.
N wherein
2Be carbonatoms n in the macromolecular compound polypropylene
3It is 7 to 11 number.
According to detection: the yield of producing Vaseline with the polypropylene waste or used plastics reaches (48-63) %); The yield of producing Vaseline with vinyon reaches (74-82) %.
The present invention is because the employing waste or used plastics is a raw material, and its raw material sources are extensively inexpensive, and by the hot gas that directly utilizes cracking to go out, liquid takes off by decolouring, filter, making, removal of impurities is once finished, thereby technology is simple, and production cost is low.Utilize negative pressure and add catalyzer, the yield of its Vaseline and quality are guaranteed.Improved the efficient of Vaseline.
Claims (1)
1. utilize the method for waste or used plastics for raw material production Vaseline, it is characterized in that waste or used plastics after cleaning is handled, drop into reactor, after adding white lime or atlapulgite or activated carbon catalyst, the cracking of heating, its cracking temperature is controlled at 320 ℃ to 480 ℃, the gas that institute's cracking generates is extracted reactor out with vacuum, its negative pressure is controlled at 0.04 to 0.12 normal atmosphere, the gas-liquid that vacuum is extracted out is after filtering, after decolouring by the decolorizer that is equipped with catalyzer such as activated carbon or atlapulgite, filter again, promptly make the Vaseline product after the cooling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96117443A CN1093162C (en) | 1996-02-08 | 1996-02-08 | Process for producing vaseline using waste plastics as raw material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96117443A CN1093162C (en) | 1996-02-08 | 1996-02-08 | Process for producing vaseline using waste plastics as raw material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1156750A CN1156750A (en) | 1997-08-13 |
| CN1093162C true CN1093162C (en) | 2002-10-23 |
Family
ID=5124299
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96117443A Expired - Fee Related CN1093162C (en) | 1996-02-08 | 1996-02-08 | Process for producing vaseline using waste plastics as raw material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1093162C (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107201245B (en) * | 2017-06-30 | 2019-05-03 | 河南地之绿环保科技有限公司 | A kind of cracking of waste plastics purification process technique |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5345894A (en) * | 1976-10-04 | 1978-04-25 | Kajima Corp | Device for handling freight in ship or the like |
| CN1095094A (en) * | 1993-10-23 | 1994-11-16 | 杨森威 | The method of producing liquid fuel by waste plastics |
| CN1114674A (en) * | 1994-07-06 | 1996-01-10 | 抚顺石化龙源科工贸总公司 | Preparation of lubricating oil base oil by using cracked oil of waste plastics |
-
1996
- 1996-02-08 CN CN96117443A patent/CN1093162C/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5345894A (en) * | 1976-10-04 | 1978-04-25 | Kajima Corp | Device for handling freight in ship or the like |
| CN1095094A (en) * | 1993-10-23 | 1994-11-16 | 杨森威 | The method of producing liquid fuel by waste plastics |
| CN1114674A (en) * | 1994-07-06 | 1996-01-10 | 抚顺石化龙源科工贸总公司 | Preparation of lubricating oil base oil by using cracked oil of waste plastics |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1156750A (en) | 1997-08-13 |
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|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |