CN205035343U - Indirect heating's rose liquid alembic - Google Patents
Indirect heating's rose liquid alembic Download PDFInfo
- Publication number
- CN205035343U CN205035343U CN201520630073.9U CN201520630073U CN205035343U CN 205035343 U CN205035343 U CN 205035343U CN 201520630073 U CN201520630073 U CN 201520630073U CN 205035343 U CN205035343 U CN 205035343U
- Authority
- CN
- China
- Prior art keywords
- heating pipe
- rose
- indirect heating
- rose liquid
- tank body
- 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
- 238000010438 heat treatment Methods 0.000 title claims abstract description 42
- 241000220317 Rosa Species 0.000 title claims abstract description 22
- 239000007788 liquid Substances 0.000 title claims abstract description 18
- 239000002184 metal Substances 0.000 claims abstract description 5
- 238000013022 venting Methods 0.000 claims description 8
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 9
- 206010037660 Pyrexia Diseases 0.000 abstract 1
- 229910000831 Steel Inorganic materials 0.000 abstract 1
- 230000002349 favourable effect Effects 0.000 abstract 1
- 239000010959 steel Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 230000000153 supplemental effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 240000004978 Rosa x damascena Species 0.000 description 1
- 235000011402 Rosa x damascena Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000000341 volatile oil Substances 0.000 description 1
Landscapes
- Cookers (AREA)
Abstract
The utility model discloses an indirect heating's rose liquid alembic, including the nonrust steel can body, its characterized in that: jar body lower part is sandwich structure: jar external wall is from the bottom spiral heating pipe that has upwards spiraled, and heating pipe upper portion sets up the air inlet, the lower part sets up the gas vent, and the heating pipe wraps up the insulating layer outward, and the insulating layer is outer sealed by metal casing. This alembic from air inlet input high -temperature steam, is discharged from the gas vent behind the heating pipe, and the heat passes through metal heating pipe and a jar body and conducts the internal rose material of jar, and steam and material be direct contact not, avoids influencing that the material produces oil and rose hydrosol's quality, and in addition, the heating pipe wraps up the insulating layer outward, is favorable to improving the utilization ratio of heat energy.
Description
Technical field
The utility model belongs to rose liquid water distilling apparatus, especially relates to a kind of rose liquid retort of indirect heating.
Background technology
Continue to use under age-old approach distills normal pressure situation due to pink damask rose always and carry out extracting fragrant volatile oil, steam directly contacts with material, and the steam of heating is after cooling, flower water in tank can be made out of proportion and affect oil yield and odor type change, and, conventional retort is insufficient to Btu utilization, and energy expenditure is large.
Summary of the invention
It is good and can make full use of the rose liquid retort of the indirect heating of heat energy that the utility model aims to provide a kind of distilling effect.
The technical solution adopted in the utility model is:
The rose liquid retort of indirect heating, comprises stainless steel tank body, and tank body lower part is sandwich structure, tank wall has upwards spiraled from bottom spiral type heated pipe, heating tube top arranges inlet mouth, bottom arranges venting port, heating tube external parcel thermofin, and thermofin is outer to be sealed by metal shell.
Further, the heating tube of tank wall spirals is highly 2/3rds of tank body; Inlet mouth and venting port are two.
According to the rose liquid retort of above-described indirect heating, tank body, heating tube and shell are 304 stainless steels; Tank volume is 3000L; Heating tube diameter 100mm, thickness 5mm.
Adopt the rose liquid retort of the indirect heating of the present utility model of above structure, the spiral type heated pipe of tank wall, avoids steam directly to contact with material, improves fuel-displaced with hydrosol quality, and heat energy is fully transmitted in tank body; Thermofin, reduces scattering and disappearing of heat energy, improves heat utilization rate; Two inlet mouth and venting port, timely supplemental heat steam, discharge cold steam, improves distillation efficiency.
Accompanying drawing explanation
Fig. 1 is the rose liquid retort structural representation of the indirect heating of the utility model embodiment.
Embodiment
Be described in detail below in conjunction with the technical scheme of accompanying drawing to the rose liquid retort of indirect heating of the present utility model.
As shown in Figure 1, the rose liquid retort of indirect heating, comprise stainless steel tank body 1, tank body 1 bottom is sandwich structure, tank body 1 outer wall 11 has upwards spiraled from bottom spiral type heated pipe 4, heating tube 4 top arranges two inlet mouths 2, bottom arranges two venting ports 3, heating tube 4 external parcel thermofin 5, and thermofin 5 is outer to be sealed by metal shell 6.
It is highly 2/3rds of tank body 1 that the heating tube 4 of tank wall 11 spirals.
Tank body 1, heating tube 4 are 304 stainless steels with shell 6; Tank body 1 volume is 3000L; Heating tube 4 diameter 100mm, thickness 5mm.
During work, tank body 1 is built with rose material to be distilled, hot steam is inputted from inlet mouth 2, steam, is discharged, in process from venting port 3 down to bottom tank body 1 through heating tube 4, the heat energy that steam carries is transferred to the material in tank body through stainless heating tube 4 and tank wall 11, thermal distillation is added to material, because steam does not directly contact with material, therefore can not affect the fuel-displaced and hydrosol quality of rose due to steam cooling.
Thermofin 5 and shell 6, be conducive to the heat keeping heating tube 4, reduce heat loss, improve heat utilization rate.
Two inlet mouths and venting port, be conducive to supplemental heat steam or the cold steam of Accelerating Removal as required, increase work efficiency.
It is more than embodiment of the present utility model; the restriction to protection domain of the present utility model must not be interpreted as; those skilled in the art should be appreciated that amendment of the present utility model or equivalent replacement, all do not depart from the protection domain of technical solutions of the utility model.
Claims (6)
1. the rose liquid retort of an indirect heating, comprise stainless steel tank body, it is characterized in that: tank body lower part is sandwich structure: tank wall has upwards spiraled from bottom spiral type heated pipe, heating tube top arranges inlet mouth, bottom arranges venting port, heating tube external parcel thermofin, thermofin is outer to be sealed by metal shell.
2. the rose liquid retort of indirect heating according to claim 1, is characterized in that: it is highly 2/3rds of tank body that the heating tube of tank wall spirals.
3. the rose liquid retort of indirect heating according to claim 1, is characterized in that: described inlet mouth and venting port are two.
4. the rose liquid retort of indirect heating according to claim 1, is characterized in that: described tank body, heating tube and shell are 304 stainless steels.
5. the rose liquid retort of indirect heating according to claim 1, is characterized in that: described tank volume is 3000L.
6. the rose liquid retort of indirect heating according to claim 1, is characterized in that: described heating tube diameter 100mm, thickness 5mm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520630073.9U CN205035343U (en) | 2015-08-20 | 2015-08-20 | Indirect heating's rose liquid alembic |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520630073.9U CN205035343U (en) | 2015-08-20 | 2015-08-20 | Indirect heating's rose liquid alembic |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205035343U true CN205035343U (en) | 2016-02-17 |
Family
ID=55294255
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520630073.9U Expired - Fee Related CN205035343U (en) | 2015-08-20 | 2015-08-20 | Indirect heating's rose liquid alembic |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205035343U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106906048A (en) * | 2017-03-29 | 2017-06-30 | 福州法莫优科机械科技有限公司 | Rosa Damascana extraction element and its application method |
-
2015
- 2015-08-20 CN CN201520630073.9U patent/CN205035343U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106906048A (en) * | 2017-03-29 | 2017-06-30 | 福州法莫优科机械科技有限公司 | Rosa Damascana extraction element and its application method |
CN106906048B (en) * | 2017-03-29 | 2023-03-17 | 福州法莫优科机械科技有限公司 | Rose essential oil extraction device and use method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN203904327U (en) | White liquor distilling apparatus | |
CN205710682U (en) | A kind of multi-functional distillation equipment of wine | |
CN205035343U (en) | Indirect heating's rose liquid alembic | |
CN204853428U (en) | Energy -efficient cast aluminium body | |
CN202909594U (en) | Novel steam-water separating tank for steam | |
CN205223164U (en) | Efficient making wine equipment | |
CN105090923B (en) | Efficient energy-saving aluminum casting body | |
CN205119797U (en) | Energy -saving melting furnace | |
CN204824834U (en) | Wine pot is evaporated to intermediate layer formula | |
CN203700458U (en) | Reduction distilling furnace for producing titanium sponge by virtue of magnesium reduction method | |
CN202792481U (en) | Multi-level layered heat exchange displacement efficient water heater | |
CN203021544U (en) | Distilled spirit steamer and distilled spirit distilling device | |
CN106861219A (en) | A kind of rose liquid alembic of indirectly heat | |
CN205090364U (en) | Spent steam waste heat utilization equipment suitable for evaporate pressure cauldron | |
CN202793121U (en) | Novel high-efficiency superconductive heat pipe flue smoke residual heat collector | |
CN203890343U (en) | Liquor distilling kettle | |
CN204187599U (en) | A kind of still kettle afterheat steam recycling device | |
CN201560226U (en) | Reactor large cover in process of producing titanium sponge with magnesium method | |
CN106867669A (en) | A kind of rose liquid extractor of two-step heating | |
CN205035344U (en) | Jar is drawed to rose essential oil negative pressure | |
CN204939444U (en) | A kind of tea wine retort | |
CN205031926U (en) | Rose liquid of two -stage heating draws jar | |
CN219323869U (en) | Methanol heating transformation device | |
CN202791979U (en) | Direct gas mixing type superheated steam generating pot | |
CN206496332U (en) | A kind of combustion furnace extracted for fir essential oil |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160217 |