CN204246850U - A kind of paraffin oil and the accurate separation system device of carrene - Google Patents
A kind of paraffin oil and the accurate separation system device of carrene Download PDFInfo
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- CN204246850U CN204246850U CN201420725529.5U CN201420725529U CN204246850U CN 204246850 U CN204246850 U CN 204246850U CN 201420725529 U CN201420725529 U CN 201420725529U CN 204246850 U CN204246850 U CN 204246850U
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- circular heating
- heating tower
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- carrene
- reboiler
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A kind of paraffin oil and the accurate separation system device of carrene, comprise reboiler, high-pressure circulation pump, circular heating tower, shower nozzle, first-stage condenser, secondary condenser and material inlet, the entrance of described high-pressure circulation pump is communicated with circular heating tower bottom, described cycle of higher pressure delivery side of pump is communicated with the entrance of reboiler, the outlet of described reboiler is communicated with the shower nozzle on circular heating tower top, described shower nozzle is positioned at the top of circular heating tower, the upper side of described circular heating tower has material inlet, the top of described circular heating tower is communicated with first-stage condenser, described first-stage condenser is communicated with secondary condenser by pipeline.The utility model adopts steam-heated mode to save energy consumption greatly.
Description
Technical field
The utility model relates to separation equipment, is specially a kind of paraffin oil and the accurate separation system device of carrene.
Background technology
In lithium battery preparation technology, when paraffin oil is separated with carrene by needs, conventional separating technology often inferior separating effect, disengaging time is long, and energy consumption is high, and labour intensity is large, brings very large inconvenience to production.
Summary of the invention
The technical problem that the utility model solves is to provide a kind of paraffin oil and the accurate separation system device of carrene, to solve the shortcoming in above-mentioned background technology.
The technical problem that the utility model solves realizes by the following technical solutions:
A kind of paraffin oil and the accurate separation system device of carrene, comprise reboiler, high-pressure circulation pump, circular heating tower, shower nozzle, first-stage condenser, secondary condenser and material inlet, the entrance of described high-pressure circulation pump is communicated with circular heating tower bottom, described cycle of higher pressure delivery side of pump is communicated with the entrance of reboiler, the outlet of described reboiler is communicated with the shower nozzle on circular heating tower top, described shower nozzle is positioned at the top of circular heating tower, the upper side of described circular heating tower has material inlet, the top of described circular heating tower is communicated with first-stage condenser, described first-stage condenser is communicated with secondary condenser by pipeline.
In the utility model, the entrance and exit place of described high-pressure circulation pump is all provided with valve.
In the utility model, described reboiler upper end has steam inlet.
In the utility model, described circular heating tower inside is provided with at least two-layer screen pack.
Beneficial effect: the utility model adopts steam-heated mode to save energy consumption greatly; Adopt the use of high-pressure circulation pump, strengthen the disposal ability of raw material greatly, within the shortest time, process qualified material; Adopt the heating function of indirect steam, avoid the pollution again of medium, more ensure that the purity of medium; Adopt two-stage cooling system, the more rational carrene by volatilization is recycled utilization, guarantees without any exhaust emissions, and reduces the cost of tail gas recycle.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
The technological means realized to make the utility model, creation characteristic, reaching object and effect is easy to understand, below in conjunction with concrete diagram, setting forth the utility model further.
See Fig. 1, the structural representation of a kind of paraffin oil and the accurate separation system device of carrene, a kind of paraffin oil and the accurate separation system device of carrene, comprise reboiler 1, high-pressure circulation pump 2, circular heating tower 3, shower nozzle 4, first-stage condenser 5, secondary condenser 6 and material inlet 7, the entrance of described high-pressure circulation pump 2 is communicated with circular heating tower 3 bottom, the outlet of described high-pressure circulation pump 2 is communicated with the entrance of reboiler 1, the outlet of described reboiler 1 is communicated with the shower nozzle 4 on circular heating tower 3 top, described shower nozzle 4 is positioned at the top of circular heating tower 3, the upper side of described circular heating tower 3 has material inlet 7, the top of described circular heating tower 3 is communicated with first-stage condenser 5, described first-stage condenser 5 is communicated with secondary condenser 6 by pipeline.The entrance and exit place of described high-pressure circulation pump 2 is all provided with valve; Described reboiler 1 upper end has steam inlet; Described circular heating tower 3 inside is provided with at least two-layer screen pack.
The boiling point of carrene: 39 DEG C, paraffin oil boiling point: 230 DEG C; During use, first paraffin oil enters circular heating tower in the mixture of carrene, closes high-pressure circulation pump, steam, open pipeline high-pressure circulation pump and circulate to material after the liquid level that medium meets the demands while charging; After the circulatory system is run, open the steam valve of reboiler, medium temperature is increased to 100 DEG C, make tower reactor inside produce air pressure; Through above systemic circulation, the carrene in solvent is after high temperature, and then volatilization enters condenser by meteorological pipeline rapidly.Carrene is changing liquid into after the process of low temperature, finally obtains qualified carrene.
The utility model adopts steam-heated function, and the mixture of recycling high-pressure pump to carrene and paraffin oil carries out the process of circular heating, finally adopts meteorological principle to be exported by the composition of carrene, finally obtains pure carrene.And carrene purity >=99.99% processed.
The utility model utilizes steam heating media, and medium, higher than the boiling point of carrene, but lower than the boiling point of paraffin oil, then to be extracted out by circulating pump and is then delivered to tower top by the temperature of medium at the bottom of tower.Structure mesohigh backflow delivery side of pump adopts gondola water faucet structure, better volatilizees to medium.
More than show and describe general principle of the present utility model and principal character and advantage of the present utility model, the technical staff of the industry should understand, the utility model is not restricted to the described embodiments, what describe in above-described embodiment and description just illustrates principle of the present utility model, under the prerequisite not departing from the utility model spirit and scope, the utility model also has various changes and modifications, these changes and improvements all fall within the scope of claimed the utility model, the claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (4)
1. a paraffin oil and the accurate separation system device of carrene, comprise reboiler, high-pressure circulation pump, circular heating tower, shower nozzle, first-stage condenser, secondary condenser and material inlet, it is characterized in that, the entrance of described high-pressure circulation pump is communicated with circular heating tower bottom, described cycle of higher pressure delivery side of pump is communicated with the entrance of reboiler, the outlet of described reboiler is communicated with the shower nozzle on circular heating tower top, described shower nozzle is positioned at the top of circular heating tower, the upper side of described circular heating tower has material inlet, the top of described circular heating tower is communicated with first-stage condenser, described first-stage condenser is communicated with secondary condenser by pipeline.
2. a kind of paraffin oil according to claim 1 and the accurate separation system device of carrene, it is characterized in that, the entrance and exit place of described high-pressure circulation pump is all provided with valve.
3. a kind of paraffin oil according to claim 1 and the accurate separation system device of carrene, it is characterized in that, described reboiler upper end has steam inlet.
4. a kind of paraffin oil according to claim 1 and the accurate separation system device of carrene, it is characterized in that, described circular heating tower inside is provided with at least two-layer screen pack.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420725529.5U CN204246850U (en) | 2014-11-28 | 2014-11-28 | A kind of paraffin oil and the accurate separation system device of carrene |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420725529.5U CN204246850U (en) | 2014-11-28 | 2014-11-28 | A kind of paraffin oil and the accurate separation system device of carrene |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204246850U true CN204246850U (en) | 2015-04-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420725529.5U Active CN204246850U (en) | 2014-11-28 | 2014-11-28 | A kind of paraffin oil and the accurate separation system device of carrene |
Country Status (1)
| Country | Link |
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| CN (1) | CN204246850U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105148550A (en) * | 2015-07-15 | 2015-12-16 | 苏州捷力新能源材料有限公司 | Dichloromethane extract liquid separation apparatus |
-
2014
- 2014-11-28 CN CN201420725529.5U patent/CN204246850U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105148550A (en) * | 2015-07-15 | 2015-12-16 | 苏州捷力新能源材料有限公司 | Dichloromethane extract liquid separation apparatus |
| CN105148550B (en) * | 2015-07-15 | 2017-06-13 | 苏州捷力新能源材料有限公司 | Dichloromethane extract separator |
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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: Paraffin oil and dichloromethane precision separation system device Effective date of registration: 20151218 Granted publication date: 20150408 Pledgee: Changde Caixin technology Company limited by guarantee Pledgor: HUNAN CHINALY NEW MATERIAL Co.,Ltd. Registration number: 2015430000043 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20161226 Granted publication date: 20150408 Pledgee: Changde Caixin technology Company limited by guarantee Pledgor: HUNAN CHINALY NEW MATERIAL Co.,Ltd. Registration number: 2015430000043 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Paraffin oil and dichloromethane precision separation system device Effective date of registration: 20170111 Granted publication date: 20150408 Pledgee: Changde Caixin technology Company limited by guarantee Pledgor: HUNAN CHINALY NEW MATERIAL Co.,Ltd. Registration number: 2017430000006 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20191227 Granted publication date: 20150408 Pledgee: Changde Caixin technology Company limited by guarantee Pledgor: HUNAN CHINALY NEW MATERIAL Co.,Ltd. Registration number: 2017430000006 |
|
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 415000 No. 11, Songlin Road, Changde economic and Technological Development Zone, Changde City, Hunan Province Patentee after: Sinoma lithium film (Changde) Co.,Ltd. Address before: 415001 north of Taolin Road, group 3, qixing'an village, Deshan Town, Changde economic and Technological Development Zone, Changde City, Hunan Province Patentee before: HUNAN CHINALY NEW MATERIAL Co.,Ltd. |