CN205517751U - Airtight consecutive reaction grease alkali refining device - Google Patents
Airtight consecutive reaction grease alkali refining device Download PDFInfo
- Publication number
- CN205517751U CN205517751U CN201620282583.6U CN201620282583U CN205517751U CN 205517751 U CN205517751 U CN 205517751U CN 201620282583 U CN201620282583 U CN 201620282583U CN 205517751 U CN205517751 U CN 205517751U
- Authority
- CN
- China
- Prior art keywords
- tank
- airtight
- jar
- alkali refining
- shaft
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- 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
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- 238000009874 alkali refining Methods 0.000 title claims abstract description 37
- 239000004519 grease Substances 0.000 title abstract description 4
- 239000000463 material Substances 0.000 claims description 17
- 239000011261 inert gas Substances 0.000 claims 2
- 238000003756 stirring Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract description 5
- 239000012295 chemical reaction liquid Substances 0.000 abstract 2
- 230000035484 reaction time Effects 0.000 abstract 2
- 239000003921 oil Substances 0.000 description 26
- 235000019198 oils Nutrition 0.000 description 26
- 229910052756 noble gas Inorganic materials 0.000 description 18
- 239000000376 reactant Substances 0.000 description 10
- 238000007599 discharging Methods 0.000 description 5
- 239000002585 base Substances 0.000 description 4
- 230000001276 controlling effect Effects 0.000 description 3
- 230000000875 corresponding Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 description 2
- 239000008158 vegetable oil Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000001105 regulatory Effects 0.000 description 1
Abstract
The utility model discloses an airtight consecutive reaction grease alkali refining device, including a jar body, the feeding valve has been offered to a jar body bottom, has offered a plurality of ejection of compact valves on the lateral wall of jar body, and the bleeder valve gate open is crossed the pipeline and is located jar ejection of compact pipeline of body top and is connected, the internal (mixing) shaft that is provided with by motor drive of jar is provided with stirring paddle leaf on. The utility model discloses an airtight consecutive reaction grease alkali refining device, the reaction liquid that mixes through with the meet a condition gets into a jar body with the velocity of flow of setting for from jar pipeline of the feed valve gate control of body bottom, react under the stirring paddle leaf's by the (mixing) shaft drive mixing effect and fix time, when being satisfied reaction time, the required time and the velocity of flow react liquid at the internal height of jar according to reacting, it correspondingly selects proximate ejection of compact valve to carry out the ejection of compact (other ejection of compact valves keep closing) when high to reach at the liquid level that mixes reaction liquid, the realization regulation and control accurate to reaction time, and have concurrently and can completely cut off air and jar body utilization ratio up to 100% advantage.
Description
Technical field
This utility model relates to oil alkali refining technical field, be specifically related to a kind of can the airtight successive reaction oil alkali refining device of timing.
Background technology
Oil alkali refining, refers to use the free fatty in alkali and in sample, and removes a kind of method of refining of other impurity of part simultaneously.Alkali refining tank for oil is production equipment important in oil and fat refining process.At present, airtight continuous alkali-refining equipment is broadly divided into 2 types, the first: bottom in and top out type, this kind equipment has and air exclusion, the advantage of tank body utilization rate 100%, but it exists response time nonadjustable shortcoming；The second, upper entering and lower leaving type, this kind of equipment has response time adjustable advantage, but it exists tank body utilization rate and is only 75%, and the shortcoming that can not completely cut off air.Therefore, it is badly in need of design one class and has isolation air, tank body utilization rate height, response time regulatable oil alkali refining device concurrently.
Utility model content
In order to overcome above-mentioned the deficiencies in the prior art or defect, the purpose of this utility model is to provide a kind of response time controllable, can completely cut off air and tank body utilization rate be up to 100% airtight successive reaction oil alkali refining device.
This utility model is to realize by following technical solution:
A kind of airtight successive reaction oil alkali refining device, including tank body, tank base offers material inlet valve, and the sidewall of tank body offers multiple discharge valve, and discharge valve is connected with the discharge pipe being located at above tank body by pipeline；It is provided with by motor-driven shaft in tank body, shaft is provided with stirrer paddle.
The operation principle of airtight successive reaction oil alkali refining device of the present utility model is: the pipeline that the mixed reaction solution meeting condition controls from the material inlet valve of tank base with the flow velocity set is entered tank body, react certain time under the stirring action of the stirrer paddle driven by shaft, reactant liquor height in tank body when being met the response time according to reaction required time and flow velocity, or obtain mixed reaction solution according to reactant liquor height in tank body when meeting the response time and reaction required time and entered the flow velocity (controlling feed rate in the case of not affecting quantity-produced at the uniform velocity) of tank body by material inlet valve, realize regulation and control accurate to the response time, liquid level at mixed reaction solution reaches to select immediate discharge valve to carry out discharging (other discharge valves remain turned-off) during corresponding height, can realize producing continuously；Wherein, discharge valve from down to up meets response time needs from short to long successively.
Wherein, described tank body is cylinder, and its radius is r(m), the flow velocity that the mixed reaction solution meeting condition enters tank body by material inlet valve is v(L/min), reaction required time is t(min), then reactant liquor height h=vt/ π r in tank body when meeting the response time2；Or, when meeting the response time, reactant liquor height of the discharge valve of discharging in tank body is h(m), reaction required time is t(min), then control mixed reaction solution and entered the flow velocity v=π r of tank body by material inlet valve2h/t。
Additionally, in order to prevent the oil sample mixing in grease alkali refining technology of described airtight successive reaction oil alkali refining device uneven, inner tank wall is additionally provided with dividing plate.
Preferably, the top of described tank body is additionally provided with noble gas valve, and noble gas valve is connected with air accumulator by pipeline.When described noble gas valve is opened in tank body, be filled with noble gas time so that noble gas height in tank body remains above the height of discharge valve, further ensures mixed reaction solution and air exclusion.
Wherein, one or more in flat paddle stirrer paddle, oblique leaf formula stirrer paddle, screw mixing blade of the stirrer paddle described shaft arranged.
If the response time is shorter needed for mixed reaction solution, can reach to increase the effect of tank body top hybrid reaction fluid-in-flux by following three kinds of modes: (1) by slightly being opened by the discharge valve of tank wall top, then can make top mixed reaction solution slowly discharge；(2) by by the pipeline of noble gas Valve controlling, being filled with appropriate noble gas in tank body, charge is on top, discharge nozzle road junction；(3) except being regulated by discharge valve or noble gas valve, oblique leaf formula stirrer paddle or screw mixing blade can also be set to by shaft upper part, lower part is set to flat paddle stirrer paddle, to reach to increase the effect of tank body top hybrid reaction fluid-in-flux, thus preferably regulate and control the response time.
Wherein, described discharge valve is arranged in parallel on tank wall, and spacing distance is equal, and discharge valve from down to up meets response time needs from short to long successively.
Wherein, described motor is arranged on tank body top, and the control switch of motor draws to get off by connecting line；The control switch of described motor at least includes open switch and speed switch.
Compared with prior art, this utility model has the advantages that
1) airtight successive reaction oil alkali refining device of the present utility model, by the pipeline that the mixed reaction solution meeting condition controls from the material inlet valve of tank base with the flow velocity set is entered tank body, react certain time under the stirring action of the stirrer paddle driven by shaft, reactant liquor height in tank body when being met the response time according to reaction required time and flow velocity, or obtain mixed reaction solution according to reactant liquor height in tank body when meeting the response time and reaction required time and entered the flow velocity of tank body by material inlet valve, liquid level at mixed reaction solution reaches to select immediate discharge valve to carry out discharging (other discharge valves remain turned-off) during corresponding height, realize regulation and control accurate to the response time.
2) airtight successive reaction oil alkali refining device of the present utility model uses the form of bottom in and top out, and reacting tank body is closed type, can completely cut off air and tank body utilization rate is up to 100%；When tank body utilization rate is up to 100%, stirrer paddle utilization rate can be improved simultaneously.
3) airtight successive reaction oil alkali refining device of the present utility model is provided with noble gas valve, when this noble gas valve is opened in tank body, be filled with noble gas time, make noble gas height in tank body remain above the height of discharge valve, further ensure mixed reaction solution and air exclusion.
4) shaft upper part is set to oblique leaf formula stirrer paddle or screw mixing blade by airtight successive reaction oil alkali refining device of the present utility model, lower part is set to flat paddle stirrer paddle, to reach to increase the effect of tank body top hybrid reaction fluid-in-flux, thus preferably regulate and control the response time.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model airtight successive reaction oil alkali refining device；
In Fig. 1: 1, tank body, 2, shaft, 3, flat paddle stirrer paddle, 4, dividing plate, 5, stirring motor, 6, material inlet valve, 7, noble gas valve, 8, discharge valve.
Fig. 2 is the structural representation of the another kind of airtight successive reaction oil alkali refining device of this utility model；
In Fig. 2: 1, tank body, 2, shaft, 3, flat paddle stirrer paddle, 4, screw mixing blade or oblique leaf formula stirrer paddle, 5, dividing plate, 6, stirring motor, 7, material inlet valve, 8, discharge valve.
Detailed description of the invention
Further illustrating this utility model below by detailed description of the invention, following example are this utility model preferably embodiment, but embodiment of the present utility model is not limited by following embodiment.
Embodiment
1
As shown in Figure 1, a kind of airtight successive reaction oil alkali refining device, including airtight tank body 1, offers material inlet valve 6 bottom tank body 1, offering multiple discharge valve 8 on the sidewall of tank body 1, discharge valve 8 is connected with the discharge pipe being located at above tank body 1 by pipeline；It is provided with the shaft 2 driven by motor 5 in tank body 1, shaft 2 is provided with stirrer paddle 3；
Described discharge valve 8 is arranged in parallel on tank body 1 sidewall, and spacing distance is equal, and discharge valve from down to up meets response time needs from short to long successively；
Described motor 5 is arranged on tank body 1 top, at least includes that the control switch of the motor 5 of open switch and speed switch draws to get off by connecting line；
Described shaft 2 upper and bottom section is disposed as flat paddle stirrer paddle 3；
The dividing plate 4 of opposing parallel setting it is additionally provided with on described tank body 1 inwall；
The top of described tank body 1 is additionally provided with noble gas valve 7, and noble gas valve 7 is connected with air accumulator by pipeline；When described noble gas valve is opened in tank body, be filled with noble gas time so that noble gas height in tank body remains above the height of discharge valve, further ensures the mixed reaction solution in tank body and air exclusion.
The operation principle of airtight successive reaction oil alkali refining device of the present utility model is: the pipeline that the mixed reaction solution meeting condition controls from the material inlet valve of tank base with the flow velocity set is entered tank body, react certain time under the stirring action of the stirrer paddle driven by shaft, reactant liquor height in tank body when being met the response time according to reaction required time and flow velocity, or obtain mixed reaction solution according to reactant liquor height in tank body when meeting the response time and reaction required time and entered the flow velocity (controlling feed rate in the case of not affecting quantity-produced at the uniform velocity) of tank body by material inlet valve, realize regulation and control accurate to the response time, liquid level at mixed reaction solution reaches to select immediate discharge valve to carry out discharging (other discharge valves remain turned-off) during corresponding height, can realize producing continuously；Wherein, discharge valve from down to up meets response time needs from short to long successively.
Wherein, described tank body is cylinder, and its radius is r(m), the flow velocity that the mixed reaction solution meeting condition enters tank body by material inlet valve is v(L/min), reaction required time is t(min), then reactant liquor height h=vt/ π r in tank body when meeting the response time2；Or, when meeting the response time, reactant liquor height of the discharge valve of discharging in tank body is h(m), reaction required time is t(min), then control mixed reaction solution and entered the flow velocity v=π r of tank body by material inlet valve2h/t。
Embodiment
2
As shown in Figure 2, a kind of airtight successive reaction oil alkali refining device, including airtight tank body 1, offers material inlet valve 6 bottom tank body 1, offering multiple discharge valve 8 on the sidewall of tank body 1, discharge valve 8 is connected with the discharge pipe being located at above tank body 1 by pipeline；It is provided with the shaft 2 driven by motor 5 in tank body 1, shaft 2 is provided with stirrer paddle 3；
When the response time of oil alkali refining is shorter in vegetable oil fine sweetening process for described airtight successive reaction oil alkali refining device, described shaft 2 upper part is set to screw mixing blade, lower part is set to flat paddle stirrer paddle, the other the same as in Example 1, to reach to increase the effect of tank body top hybrid reaction fluid-in-flux, thus preferably regulate and control the response time.
Embodiment
3
A kind of airtight successive reaction oil alkali refining device, including airtight tank body 1, offers material inlet valve 6 bottom tank body 1, the sidewall of tank body 1 offers multiple discharge valve 8, and discharge valve 8 is connected with the discharge pipe being located at above tank body 1 by pipeline；It is provided with the shaft 2 driven by motor 5 in tank body 1, shaft 2 is provided with stirrer paddle 3；
When the response time of oil alkali refining is shorter in vegetable oil fine sweetening process for described airtight successive reaction oil alkali refining device, described shaft 2 upper part is set to oblique leaf formula stirrer paddle, lower part is set to flat paddle stirrer paddle, the other the same as in Example 2, to reach to increase the effect of tank body top hybrid reaction fluid-in-flux, thus preferably regulate and control the response time.
Claims (8)
1. an airtight successive reaction oil alkali refining device, including tank body (1), it is characterized in that, tank body (1) bottom offers material inlet valve (6), offering multiple discharge valve (8) on the sidewall of tank body (1), discharge valve (8) is connected with the discharge pipe being located at tank body (1) top by pipeline；It is provided with the shaft (2) driven by motor (5) in tank body (1), shaft (2) is provided with stirrer paddle (3).
Airtight successive reaction oil alkali refining device the most according to claim 1, it is characterised in that be additionally provided with dividing plate (4) on described tank body (1) inwall.
Airtight successive reaction oil alkali refining device the most according to claim 2, it is characterised in that described dividing plate (4) opposing parallel setting.
Airtight successive reaction oil alkali refining device the most according to claim 1, it is characterised in that the top of described tank body (1) is additionally provided with inert gas valve (7), inert gas valve (7) is connected with air accumulator by pipeline.
Airtight successive reaction oil alkali refining device the most according to claim 1, it is characterised in that one or more in flat paddle stirrer paddle, oblique leaf formula stirrer paddle, screw mixing blade of the upper stirrer paddle (3) arranged of described shaft (2).
The most airtight successive reaction oil alkali refining device, it is characterized in that, described shaft (2) upper part is set to one or more in flat paddle stirrer paddle, oblique leaf formula stirrer paddle or screw mixing blade, and described shaft (2) lower part is set to flat paddle stirrer paddle.
Airtight successive reaction oil alkali refining device the most according to claim 1, it is characterised in that described discharge valve (8) is arranged in parallel on tank body (1) sidewall, and spacing distance is equal.
Airtight successive reaction oil alkali refining device the most according to claim 1, it is characterised in that described motor (5) is arranged on tank body (1) top, the control switch of motor (5) draws to get off by connecting line；The control switch of described motor (5) at least includes open switch and speed switch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620282583.6U CN205517751U (en) | 2016-04-07 | 2016-04-07 | Airtight consecutive reaction grease alkali refining device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620282583.6U CN205517751U (en) | 2016-04-07 | 2016-04-07 | Airtight consecutive reaction grease alkali refining device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205517751U true CN205517751U (en) | 2016-08-31 |
Family
ID=57141794
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620282583.6U Expired - Fee Related CN205517751U (en) | 2016-04-07 | 2016-04-07 | Airtight consecutive reaction grease alkali refining device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205517751U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105597653A (en) * | 2016-04-07 | 2016-05-25 | 广东卓原新材料科技有限公司 | Sealed continuous reaction type grease alkali refining device |
-
2016
- 2016-04-07 CN CN201620282583.6U patent/CN205517751U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105597653A (en) * | 2016-04-07 | 2016-05-25 | 广东卓原新材料科技有限公司 | Sealed continuous reaction type grease alkali refining device |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20180407 |