CN203382719U - Production line for cracking, distillation and regeneration of waste oil - Google Patents
Production line for cracking, distillation and regeneration of waste oil Download PDFInfo
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- CN203382719U CN203382719U CN201320492458.4U CN201320492458U CN203382719U CN 203382719 U CN203382719 U CN 203382719U CN 201320492458 U CN201320492458 U CN 201320492458U CN 203382719 U CN203382719 U CN 203382719U
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- storage tank
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Abstract
The utility model discloses a production line for the cracking, distillation and regeneration of waste oil, which is composed of a raw material storage tank (1), a pump (1-1), a thin film evaporator (2), a heavy oil collecting tank (2-1), a catalytic reactor (6), a finished lubricant collecting and storage tank (7), a thermal separator (3), a cooler (4) and a product collecting and storage tank (5). The production line disclosed by the utility model has the advantages that because the catalytic reactor for cracking oil gas is added, after oil gas subjected to cracking is acted by a catalyst, the combination of oil molecules is reformed, so that the quality classification of products is clear, the quality of products is greatly improved, products are not required to be subjected to secondary treating, and the overall yield is increased.
Description
Technical field
The utility model relates to waste oil cracking field, is specifically related to a kind of waste oil cracking distillation regeneration production line.
Background technology
At present, technology of waste oil regenerating has various ways, and existing waste lubricating oil reclaims the pyrolysis recycle line production system without the catalytic polymerization reactor, and general reactor only has import and outlet, and product separation is unclear.
The utility model content
The purpose of this utility model has various ways for current technology of waste oil regenerating exactly, and existing waste lubricating oil reclaims the pyrolysis recycle line production system without the catalytic polymerization reactor, general reactor only has import and outlet, the deficiency that product separation is unclear, and a kind of waste oil cracking distillation regeneration production line is provided.
The utility model is by raw material storage tank, pump, thin-film evaporator, the heavy oil holding tank, catalyticreactor, finished lube is collected storage tank, heat separator, water cooler and product-collecting storage tank form, the discharge port of raw material storage tank communicates with the import of pump by pipeline, pump outlet communicates with the import of thin-film evaporator by pipeline, the concentrated material outlet of thin-film evaporator communicates with the import of heavy oil holding tank, the vapour outlet of thin-film evaporator communicates with the oil and gas import of catalyticreactor by guide pipe, the import that the outlet at bottom of catalyticreactor is collected storage tank by pipeline with finished lube communicates, the oil gas vent of catalyticreactor communicates with the product-collecting storage tank by pipeline, heat separator and water cooler are arranged on pipeline respectively.
The utility model advantage is: increased the catalyticreactor of cracking oil gas, made oil gas after cracking by the effect of catalyzer, the combination of having reformed oil molecule, make the quality product classification clear, quality product improves greatly, and product, again without secondary treatment, has increased overall yield.
the accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Embodiment
As shown in Figure 1, the utility model is by raw material storage tank 1, pump 1-1, thin-film evaporator 2, heavy oil holding tank 2-1, catalyticreactor 6, finished lube is collected storage tank 7, heat separator 3, water cooler 4 and product-collecting storage tank 5 form, the discharge port of raw material storage tank 1 communicates with the import of pump 1-1 by pipeline, the outlet of pump 1-1 communicates with the import of thin-film evaporator 2 by pipeline, the concentrated material outlet of thin-film evaporator 2 communicates with the import of heavy oil holding tank 2-1, the vapour outlet of thin-film evaporator 2 communicates with the oil and gas import of catalyticreactor 6 by guide pipe, the import that the outlet at bottom of catalyticreactor 6 is collected storage tank 7 by pipeline with finished lube communicates, the oil gas vent of catalyticreactor 6 communicates with product-collecting storage tank 5 by pipeline 6-1, heat separator 3 and water cooler 4 are arranged on respectively on pipeline 6-1.
Mode of operation: the waste oil in raw material storage tank 1 is pumped to thin-film evaporator 2 by pump 1-1, oil molecule after thin-film evaporator 2 cracking enters in catalyticreactor 6 through the restructuring of molecule building-up reactions, uncracked heavy oil molecules enters to heavy oil holding tank 2-1 from the concentrated material exit of thin-film evaporator 2, reacted heavy oil molecules is collected finished lube by reactor bottom and is collected in storage tank 7, the oil molecule distilled out at catalyticreactor 6 tops is collected as respectively diesel oil and light-weight fuel oil by heat separator 3 and water cooler 4, when collecting certain liquid level respectively with being pumped in product-collecting storage tank 5.
Claims (1)
1. the regeneration production line is distilled in a waste oil cracking, it is characterized in that it is by raw material storage tank (1), pump (1-1), thin-film evaporator (2), heavy oil holding tank (2-1), catalyticreactor (6), finished lube is collected storage tank (7), heat separator (3), water cooler (4) and product-collecting storage tank (5) form, the discharge port of raw material storage tank (1) communicates with the import of pump (1-1) by pipeline, the outlet of pump (1-1) communicates with the import of thin-film evaporator (2) by pipeline, the concentrated material outlet of thin-film evaporator (2) communicates with the import of heavy oil holding tank (2-1), the vapour outlet of thin-film evaporator (2) communicates with the oil and gas import of catalyticreactor (6) by guide pipe, the import that the outlet at bottom of catalyticreactor (6) is collected storage tank (7) by pipeline with finished lube communicates, the oil gas vent of catalyticreactor (6) communicates with product-collecting storage tank (5) by pipeline (6-1), heat separator (3) and water cooler (4) are arranged on respectively on pipeline (6-1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320492458.4U CN203382719U (en) | 2013-08-13 | 2013-08-13 | Production line for cracking, distillation and regeneration of waste oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320492458.4U CN203382719U (en) | 2013-08-13 | 2013-08-13 | Production line for cracking, distillation and regeneration of waste oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203382719U true CN203382719U (en) | 2014-01-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320492458.4U Expired - Lifetime CN203382719U (en) | 2013-08-13 | 2013-08-13 | Production line for cracking, distillation and regeneration of waste oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203382719U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607927A (en) * | 2019-01-25 | 2019-04-12 | 江苏苏纯环保科技有限公司 | A kind of method that the refinery oil product of oil-containing dangerous waste recycles |
-
2013
- 2013-08-13 CN CN201320492458.4U patent/CN203382719U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607927A (en) * | 2019-01-25 | 2019-04-12 | 江苏苏纯环保科技有限公司 | A kind of method that the refinery oil product of oil-containing dangerous waste recycles |
| CN109607927B (en) * | 2019-01-25 | 2022-09-20 | 江苏苏纯环保科技有限公司 | Method for recycling refined and chemical oil products containing hazardous oil wastes |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Production line for waste oil pyrolysis, distillation and regeneration Effective date of registration: 20180222 Granted publication date: 20140108 Pledgee: Branch Bank of Industrial Commercial Bank of China Ltd Jingmen Petrochemical Industrial Zone Pledgor: HUBEI PATRIOTIC PETROCHEMICAL CO., LTD. Registration number: 2018420000006 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |