CN105059764A - Heptanes liquefaction outflow device - Google Patents
Heptanes liquefaction outflow device Download PDFInfo
- Publication number
- CN105059764A CN105059764A CN201510399565.6A CN201510399565A CN105059764A CN 105059764 A CN105059764 A CN 105059764A CN 201510399565 A CN201510399565 A CN 201510399565A CN 105059764 A CN105059764 A CN 105059764A
- Authority
- CN
- China
- Prior art keywords
- liquefaction
- heptane
- chamber
- delivery line
- 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.)
- Granted
Links
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical class CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 title claims abstract description 116
- 238000009413 insulation Methods 0.000 claims description 14
- 238000001816 cooling Methods 0.000 claims description 12
- 239000003983 inhalation anesthetic agent Substances 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 6
- 238000007789 sealing Methods 0.000 claims description 4
- 239000007788 liquid Substances 0.000 abstract description 9
- 230000000694 effects Effects 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000032683 aging Effects 0.000 description 1
- 230000003487 anti-permeability effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Abstract
The invention provides a Heptanes liquefaction outflow device comprising a volatilization pot, a liquefaction device and an outflow mechanism; the volatilization pot comprises a pot body and a volatilization device arranged on a side wall of the pot body; the liquefaction device comprises a liquefaction plate and a lead out pipe connected with an exit of the pot body; the liquefaction plate is in a spiral shape and axially fixed along the lead out pipe, and connected with the lead out pipe; the outflow mechanism comprises an outflow pump and an inverted valve, and is connected with the lead out pipe through the inverted valve. The Heptanes liquefaction outflow device keeps the stored heptanes in a volatilization gas state, so heptanes is easy in storage; the heptanes is liquefied into a liquid state when being used, and removal is more accurate; the Heptanes liquefaction outflow device is simple in structure, and low in production cost and usage cost.
Description
Technical field
The invention belongs to liquefying plant field, be specifically related to a kind of liquefaction bleeder for heptane.
Background technology
Heptane is a kind of colourless volatile liquid, is commonly used for the standard of octane number determination, solvent, and for the preparation of organic synthesis, experiment reagent, therefore heptane is present in laboratory and chemical enterprise in a large number.Due to the highly volatile characteristic of heptane, heptane is usually in the gaseous state of volatilization when storing, and in order to can the consumption of accurate heptane when taking, heptane needs the nonvolatile state of maintenance liquid, existing method is lowered the temperature to the storage ambient of heptane, makes to keep liquid state when taking.But this kind of method needs a large amount of energy to ensure cooling, and energy consumption is larger.
Therefore, developing a kind of device that can realize ensureing when heptane is taken the non-volatile state of liquid is those skilled in the art institute urgent need to solve the problem.
Summary of the invention
For solving the problem, the invention discloses a kind of liquefaction bleeder for heptane.
In order to achieve the above object, the invention provides following technical scheme:
For a liquefaction bleeder for heptane, comprise Volatile anesthetic, liquefying plant and flow out mechanism; Volatile anesthetic comprises tank body and volatilization device; Volatilization device is installed in the sidewall of tank body; Liquefying plant comprises liquefaction dish and delivery line; Delivery line is connected with the outlet of tank body; Liquefaction dish in the shape of a spiral along the axial restraint of delivery line, and is connected with delivery line; Flow out mechanism and comprise efflux pump and boiler check valve; Efflux pump is connected with delivery line by boiler check valve.
The invention provides a kind of liquefaction bleeder for heptane, be made up of Volatile anesthetic, liquefying plant and outflow structure.Volatilization, for storing heptane and promoting that its volatilization stores for gaseous state, being that the heptane of gaseous state extracts in liquefying plant by flowing out structure, eventually passing the liquefaction outflow of liquefying plant by Volatile anesthetic subsequently.
Volatile anesthetic in the present invention is made up of tank body and volatilization device, and heptane is stored among tank body, is provided with volatilization device in the sidewall of tank body, for keeping the volatileness of tank interior heptane.Liquefying plant in the present invention coils by liquefying and delivery line forms, and wherein liquefaction dish is in the shape of a spiral along the axial restraint of delivery line, and liquefaction dish is connected with delivery line; The heptane of gaseous state, by after extraction in tank body, arrives in liquefaction dish along delivery line and is liquefied as liquid heptane.Outflow mechanism in the present invention is made up of efflux pump and boiler check valve, efflux pump is used for the heptane of gaseous state to extract out from tank body, and by being provided with boiler check valve, prevent from extracting and the liquid heptane liquefied returns in tank body along delivery line and liquefaction dish.
As preferably, liquefaction dish comprises heptane chamber, liquefaction chamber and cooling layer from inside to outside successively; It is protruding that heptane chamber is provided with heptane chamber along its hand of spiral, and its top and bottom are all connected with delivery line; Heptane chamber is included in wherein by liquefaction chamber; Cooling layer is electronic refrigerating sheet, is affixed on the outside face in liquefaction chamber.
Liquefaction dish in the present invention is made up of heptane chamber, liquefaction chamber and cooling layer from inside to outside successively; Heptane chamber is used for heptane by the transformation of gaseous state to liquid state; Liquefaction chamber is used for carrying out cooling liquefaction to heptane chamber; Cooling layer is for keeping the low-temperature condition in liquefaction chamber; Wherein heptane chamber to be provided with heptane chamber along its hand of spiral protruding, to increase heptane chamber and the area of contact in liquefaction chamber, promote that gaseous state heptane wherein liquefies; And use electronic refrigerating sheet as cooling layer, noiseless during its work, high without wearing and tearing, reliability, action effect is good, and its size is little, lightweight, is applicable to Small And Medium Capacity of the present invention and undersized running environment.
As preferably, volatilization device is heating cushion; And the outside of tank body is also provided with heat-insulation layer.
Volatilization device in the present invention is chosen as heating cushion, improving temperature in tank body by arranging heating cushion, promote that the heptane in tank body volatilizees, and the outside of tank body being also enclosed with heat-insulation layer, for keeping the temperature in tank body, reduce operating temperature and the duration of heating cushion.
As preferably, heat-insulation layer is cystosepiment heat-insulation layer.
Heat-insulation layer in the present invention is chosen as cystosepiment heat-insulation layer, and cystosepiment has certain insulation effect, and its absorptivity is low, anti-permeability good, corrosion stability and ageing-resistant performance excellent.
As preferably, delivery line is in the part sealing between the top of liquefaction dish and bottom.
In the present invention, delivery line is in the partial design between the top of liquefaction dish and bottom is sealing, namely efflux pump by gaseous state heptane by extracting in tank body after to delivery line, can flow in liquefaction dish with the delivery line place of being connected along the top of liquefaction dish, liquefy, the bottom of being coiled by liquefaction is again connected with delivery line and flows out, and guarantees arrive in liquefaction dish after gaseous state heptane can extract from tank body to liquefy.
Compared with prior art, beneficial effect is in the present invention: keep volatilization gas state during (1) storage, be easy to storage; (2) when taking, liquefaction is liquid state, takes more accurate; (3) simple, the productive costs of structure and use cost low.
Accompanying drawing explanation
Fig. 1, structural representation of the present invention;
The structural representation of liquefaction dish in Fig. 2, the present invention;
The section drawing of Volatile anesthetic in Fig. 3, the present invention.
Reference numerals list: tank body 1, volatilization device 2, liquefaction dish 3, delivery line 4, efflux pump 5, boiler check valve 6, heptane chamber 7, liquefaction chamber 8, cooling layer 9, heat-insulation layer 10.
Detailed description of the invention
Below with reference to specific embodiment, technical scheme provided by the invention is described in detail, following detailed description of the invention should be understood and be only not used in for illustration of the present invention and limit the scope of the invention.
Be illustrated in figure 1 structural representation of the present invention, the present invention is a kind of liquefaction bleeder for heptane, comprises Volatile anesthetic, liquefying plant and flows out mechanism.
Volatile anesthetic comprises tank body 1 and volatilization device 2; As shown in Figure 3, volatilization device 2 is installed in the sidewall of tank body 1, and volatilization device 2 is heating cushion; And the outside of tank body 1 is also provided with heat-insulation layer 10, heat-insulation layer 10 is chosen as cystosepiment heat-insulation layer.
Liquefying plant comprises liquefaction dish 3 and delivery line 4; Delivery line 4 is connected with the outlet of tank body 1; Liquefaction dish 3 in the shape of a spiral along the axial restraint of delivery line 4, and is connected with delivery line 4, and delivery line 4 is in the part sealing between the top of liquefaction dish 3 and bottom; As shown in Figure 2, change dish 3 comprises heptane chamber 7, liquefaction chamber 8 and cooling layer 9 from inside to outside successively; It is protruding that heptane chamber 7 is provided with heptane chamber along its hand of spiral, and its top and bottom are all connected with delivery line 4; Heptane chamber 7 is included in wherein by liquefaction chamber 8; Cooling layer 9 is electronic refrigerating sheet, is affixed on the outside face in liquefaction chamber 8.
Flow out mechanism and comprise efflux pump 5 and boiler check valve 6; Efflux pump 5 is connected with delivery line 4 by boiler check valve 6.
Finally it should be noted that, above embodiment is only in order to illustrate technical scheme of the present invention and non-limiting technical scheme, those of ordinary skill in the art is to be understood that, those are modified to technical scheme of the present invention or equivalent replacement, and do not depart from aim and the scope of the technical program, all should be encompassed in the middle of right of the present invention.
Claims (5)
1. for a liquefaction bleeder for heptane, it is characterized in that: comprise Volatile anesthetic, liquefying plant and flow out mechanism; Described Volatile anesthetic comprises tank body (1) and volatilization device (2); Described volatilization device (2) is installed in the sidewall of tank body (1); Described liquefying plant comprises liquefaction dish (3) and delivery line (4); Described delivery line (4) is connected with the outlet of tank body (1); Described liquefaction dish (3) in the shape of a spiral along the axial restraint of delivery line (4), and is connected with delivery line (4); Described outflow mechanism comprises efflux pump (5) and boiler check valve (6); Described efflux pump (5) is connected with delivery line (4) by boiler check valve (6).
2. a kind of liquefaction bleeder for heptane according to claim 1, is characterized in that: described liquefaction dish (3) comprises heptane chamber (7), liquefaction chamber (8) and cooling layer (9) from inside to outside successively; It is protruding that described heptane chamber (7) is provided with heptane chamber along its hand of spiral, and its top and bottom are all connected with delivery line (4); Heptane chamber (7) are included in wherein by described liquefaction chamber (8); Described cooling layer (9) is electronic refrigerating sheet, is affixed on the outside face of liquefaction chamber (8).
3. a kind of liquefaction bleeder for heptane according to claim 1, is characterized in that: described volatilization device (2) is heating cushion; And the outside of tank body (1) is also provided with heat-insulation layer (10).
4. a kind of liquefaction bleeder for heptane according to claim 3, is characterized in that: described heat-insulation layer (10) is cystosepiment heat-insulation layer.
5. a kind of liquefaction bleeder for heptane according to claim 1, is characterized in that: described delivery line (4) is in the part sealing between the top of liquefaction dish (3) and bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510399565.6A CN105059764B (en) | 2015-07-09 | 2015-07-09 | Liquefaction bleeder for heptane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510399565.6A CN105059764B (en) | 2015-07-09 | 2015-07-09 | Liquefaction bleeder for heptane |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105059764A true CN105059764A (en) | 2015-11-18 |
| CN105059764B CN105059764B (en) | 2017-12-22 |
Family
ID=54489360
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510399565.6A Active CN105059764B (en) | 2015-07-09 | 2015-07-09 | Liquefaction bleeder for heptane |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105059764B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3600319A (en) * | 1968-06-25 | 1971-08-17 | Procter & Gamble | Process for application of enzymes to spray-dried detergent granules |
| JPS58205532A (en) * | 1982-05-26 | 1983-11-30 | Nippon Atom Ind Group Co Ltd | Fluid mixing container |
| CN201377680Y (en) * | 2009-01-20 | 2010-01-06 | 山东兄弟科技股份有限公司 | Saturated liquid gasifying device |
| CN203439521U (en) * | 2013-07-09 | 2014-02-19 | 南京荣欣化工有限公司 | Volatilization-proof device of propionaldehyde storage tank |
-
2015
- 2015-07-09 CN CN201510399565.6A patent/CN105059764B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3600319A (en) * | 1968-06-25 | 1971-08-17 | Procter & Gamble | Process for application of enzymes to spray-dried detergent granules |
| JPS58205532A (en) * | 1982-05-26 | 1983-11-30 | Nippon Atom Ind Group Co Ltd | Fluid mixing container |
| CN201377680Y (en) * | 2009-01-20 | 2010-01-06 | 山东兄弟科技股份有限公司 | Saturated liquid gasifying device |
| CN203439521U (en) * | 2013-07-09 | 2014-02-19 | 南京荣欣化工有限公司 | Volatilization-proof device of propionaldehyde storage tank |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105059764B (en) | 2017-12-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103486755B (en) | A kind of carbon dioxide overlapping-type commercial refrigeration system | |
| CN203979867U (en) | LNG low-temperature storage tank system | |
| CN202453746U (en) | Automatic oil level regulating system of transformer | |
| CN203743823U (en) | Low-evaporation-rate constant-temperature low-temperature liquid storage tank | |
| CN105059764A (en) | Heptanes liquefaction outflow device | |
| CN102058998A (en) | Heat pump type liquid-solid extraction device | |
| CN106499937B (en) | Water-sealed double-layer constant-pressure gas storage system for compressed air energy storage | |
| CN203478758U (en) | Ammonia liquid separator | |
| CN203964431U (en) | A kind of carbon dioxide refrigeration apparatus structure | |
| CN104132239B (en) | A kind of cryogenic gas condensation cycle system and method | |
| CN104567060A (en) | Thermal siphon oil cooling system | |
| CN204187824U (en) | There is the Teat pump boiler of air injection enthalpy-increasing | |
| CN102692149A (en) | Vessel of a heat storage and release apparatus, assembly of heat storage and release, and energy production plant | |
| CN205316034U (en) | Cold volume system of nitrogen gas | |
| CN105526490A (en) | Liquefied natural gas storage and conveying tank | |
| CN104019591A (en) | Novel ammonia refrigeration oil collector | |
| CN204421420U (en) | A kind of New-style refrigeration house condensation heat phase transformation recovery system | |
| CN203687642U (en) | Liquid nitrogen water circulation device | |
| CN104329561A (en) | System and method for producing liquefied natural gas by virtue of liquid nitrogen | |
| JP5839669B2 (en) | Liquefied gas container | |
| CN101430043A (en) | Ammonia circulating vaporization method and its electric heating carburetor | |
| CN203533190U (en) | Tank-pump integrated structure used for LNG filling station | |
| CN105465377B (en) | A kind of dismountable LNG storage tank shaft bottom valve | |
| CN108369122B (en) | The estimating method of gas discharge amount | |
| CN206019081U (en) | A kind of medium-sized low-temperature cooling fluid circulating pump |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Liquefaction effluent device for heptane Effective date of registration: 20240103 Granted publication date: 20171222 Pledgee: China Postal Savings Bank Co.,Ltd. Lai'an County Branch Pledgor: CHUZHOU RUNDA SOLVENTS Co.,Ltd. Registration number: Y2024980000220 |