CN205035338U - Lithium soap base grease production system - Google Patents
Lithium soap base grease production system Download PDFInfo
- Publication number
- CN205035338U CN205035338U CN201520826302.4U CN201520826302U CN205035338U CN 205035338 U CN205035338 U CN 205035338U CN 201520826302 U CN201520826302 U CN 201520826302U CN 205035338 U CN205035338 U CN 205035338U
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- China
- Prior art keywords
- pipeline
- communicated
- cauldron
- saponification
- blending
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Abstract
The utility model relates to a lithium soap base grease's production system, including the saponification cauldron, blending cauldron and degassing tank, the outside cover of saponification cauldron is equipped with the heating cavity, pipeline and base oil import intercommunication are passed through to the upper portion of saponification cauldron, saponification cauldron upper portion still is provided with the batching pipe, the lower part of saponification cauldron pass through the pipeline behind pump no. 1 with the upper portion intercommunication of blending cauldron, compressed air inlet passes through the entry intercommunication of pipeline and saponification cauldron and pump no. 1, be equipped with cooling device in the blending cauldron, cooling device cooling water inlet pipe and the cooling water outlet pipe intercommunication outside with the blending cauldron of blending cauldron, pipeline and base oil import intercommunication are passed through to the upper portion of blending cauldron, the lower part of blending cauldron is provided with the discharge gate, the discharge gate passes through the pipeline through the upper portion intercommunication of filter with the degassing tank, the outside of degassing tank is provided with heating cavity, the lower part of degassing tank pass through the pipeline behind pump no. 2 with the product outlet intercommunication. The utility model provides a lithium soap base grease production system, but pressure saponification and blending are suitable for the industrial production.
Description
Technical field
The utility model relates to a kind of lithium soap grease production system.
Background technology
Lithium soap grease is by hydroxy fatty acid lithium soap multiviscosisty mineral oil and adds the modulation of the multiple additives such as the multiple extreme-pressure anti-wear such as antioxygen, antirust, anti-corrosive and form.Lithium soap grease has excellent water resisting property, mechanical stability, resistance to extreme pressure and antiwear behavior, water-repellancy and pumping, rust-preventing characteristic and oxidation stability.Lithium soap grease, under exceedingly odious operational condition, can also play its super tall and erect lubrication usefulness.Produce in the process of lubricating grease at atmospheric kettle, the factor affecting saponification reaction effect is a lot, the composition of the concentration of situation about contacting each other as the concentration of temperature of reaction, reactant, reaction times, feeding sequence, reactant, churned mechanically speed, alkaloids, fat or lipid acid and basic oil composition etc.
Utility model content
Technical problem to be solved in the utility model is to provide the production system can carrying out a kind of lithium soap grease of saponification reaction under higher pressure.
The technical scheme that the utility model solves the problems of the technologies described above is as follows: a kind of production system of lithium soap grease, comprise saponification still, blending kettle and degassing vessel, described saponification still outer cover is provided with heated chamber, described heated chamber side is communicated with heat conductive oil inlet by pipeline, the opposite side of described heated chamber is by pipeline and thermal oil outlet, the top of described saponification still is provided with agitator one, the top of described saponification still is by pipeline and base oil inlet communication, described saponification still top is also provided with batching pipe, the bottom of described saponification still is communicated with the top of described blending kettle after pump one by pipeline, described compressed air inlet is communicated with by the entrance of pipeline with described saponification still and pump one, refrigerating unit is provided with in described blending kettle, the refrigerating unit of described blending kettle is communicated with cooling water outlet pipe with the cooling water inlet pipe of blending kettle outside, the top of described blending kettle is by pipeline and base oil inlet communication, the top of described blending kettle is also provided with agitator three, the bottom of described blending kettle is provided with discharge port, described discharge port is communicated with by the entrance of pipe-and-filter, the outlet of described strainer is communicated with the top of degassing vessel by pipeline, described compressed air inlet is communicated with by the entrance of pipeline with described discharge port and described strainer, the pipeline that the top of described degassing vessel is also provided with blow-down pipe and is communicated with vacuum pumping opening, the outer setting of described degassing vessel has heating cavities, the side of described heating cavities is communicated with heat conductive oil inlet by pipeline, the opposite side of described heating cavities is by pipeline and thermal oil outlet, the bottom of described degassing vessel is communicated with product outlet after pump two by pipeline, described compressed air inlet is communicated with the bottom of described degassing vessel and the entrance of described pump two by pipeline.
The production system of the lithium soap grease that the utility model provides, comprise saponification still, blending kettle and degassing vessel, particularly also comprise pipelines such as connecting charging line between these equipment and heating, cooling and pressurization, wherein compressed air inlet and connected pipeline thereof not only can in production system before reinforced, reinforced after pipe is swept to the pipeline in production system, also can need to provide suitable pressure to saponification still and blending kettle according to technique, ensure good saponification and blending effect, whole production system design safety is reasonable, is suitable for suitability for industrialized production.
On the basis of technique scheme, the utility model can also have following improvement.
Further, the bottom of described saponification still is also provided with agitator two.Saponification still is provided with two, top and the bottom agitator, can ensure the mixing of good material during reaction and good heat-transfer effect, make saponification reaction more abundant.
Further, the pipeline between the heated chamber of described saponification still and described heat conductive oil inlet is two pipelines arranged side by side, and the pipeline between the heated chamber of described saponification still and described thermal oil export is two pipelines arranged side by side.Arrange arranged side by side two and want pipeline, when one of them blocks, another can normally work, and guarantees to produce and carries out smoothly.
Further, described blending kettle bottom is also provided with discharge port for subsequent use.When discharge port breaks down, discharge port for subsequent use can be used, prevent the fault because of discharge port from causing material to stop in blending kettle for a long time and cause greater loss.
Further, the top of described degassing vessel is provided with agitator four.The top of degassing vessel arranges agitator and can stir material when degassed, makes the better effects if of the gas removal in material.
Accompanying drawing explanation
The schematic diagram of a kind of lithium soap grease production system that Fig. 1 provides for the utility model;
In accompanying drawing, the list of parts representated by each label is as follows:
1. base oil import; 2. heat conductive oil inlet; 3. thermal oil outlet; 4. compressed air inlet; 5. product outlet; 6. saponification still; 7. blending kettle; 8. degassing vessel; 9. strainer; 10. vacuum pumping opening; 11. pumps one; 12. agitators one; 13. agitators two; 14. agitators three; 15. agitators four; 16. batching pipes; 17. blow-down pipes; 18. pumps two;
Embodiment
Be described principle of the present utility model and feature below in conjunction with accompanying drawing, example, only for explaining the utility model, is not intended to limit scope of the present utility model.
As shown in Figure 1, the utility model provides a kind of production system of lithium soap grease, comprise saponification still 6, blending kettle 7 and degassing vessel 8, described saponification still 6 outer cover is provided with heated chamber, described heated chamber side is communicated with heat conductive oil inlet 2 by pipeline, the opposite side of described heated chamber exports 3 by pipeline and thermal oil and is communicated with, the top of described saponification still 6 is provided with agitator 1, the top of described saponification still 6 is communicated with base oil import 1 by pipeline, described saponification still 6 top is also provided with batching pipe 16, the bottom of described saponification still 6 is communicated with the top of described blending kettle 7 after pump 1 by pipeline, described compressed air inlet 4 is communicated with by the entrance of pipeline with described saponification still 6 and pump 1, refrigerating unit is provided with in described blending kettle 7, the refrigerating unit of described blending kettle 7 is communicated with cooling water outlet pipe with the cooling water inlet pipe of blending kettle 7 outside, the top of described blending kettle 7 is communicated with base oil import 1 by pipeline, the top of described blending kettle 7 is also provided with agitator 3 14, the bottom of described blending kettle 7 is provided with discharge port, described discharge port is communicated with by the entrance of pipe-and-filter 9, the outlet of described strainer 9 is communicated with by the top of pipeline with degassing vessel 8, described compressed air inlet 4 is communicated with by the entrance of pipeline with described discharge port and described strainer 9, the pipeline that the top of described degassing vessel 8 is also provided with blow-down pipe 17 and is communicated with vacuum pumping opening 10, the outer setting of described degassing vessel 8 has heating cavities, the side of described heating cavities is communicated with heat conductive oil inlet 2 by pipeline, the opposite side of described heating cavities exports 3 by pipeline and thermal oil and is communicated with, the bottom of described degassing vessel 8 is communicated with product outlet 5 after pump 2 18 by pipeline, described compressed air inlet 4 is communicated with the bottom of described degassing vessel 8 and the entrance of described pump 2 18 by pipeline.
Further, the bottom of described saponification still 6 is also provided with agitator 2 13.
Further, the pipeline between the heated chamber of described saponification still 6 and described heat conductive oil inlet 2 is two pipelines arranged side by side, and the heated chamber of described saponification still 6 and the described thermal oil pipeline exported between 3 is two pipelines arranged side by side.
Further, described blending kettle 7 bottom is also provided with discharge port for subsequent use.
Further, the top of described degassing vessel 8 is provided with agitator 4 15.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
1. the production system of a lithium soap grease, it is characterized in that, comprise saponification still (6), blending kettle (7) and degassing vessel (8), described saponification still (6) outer cover is provided with heated chamber, described heated chamber side is communicated with heat conductive oil inlet (2) by pipeline, the opposite side of described heated chamber is imported and exported (3) by pipeline with thermal oil and is communicated with, the top of described saponification still (6) is provided with agitator one (12), the top of described saponification still (6) is communicated with base oil import (1) by pipeline, described saponification still (6) top is also provided with batching pipe (16), the bottom of described saponification still (6) is communicated with the top of described blending kettle (7) after pump one (11) by pipeline, described compressed air inlet (4) is communicated with by the entrance of pipeline with described saponification still (6) and pump one (11), described blending kettle is provided with refrigerating unit in (7), the cooling water inlet pipe that the refrigerating unit of described blending kettle (7) is outside with blending kettle (7) is communicated with cooling water outlet pipe, the top of described blending kettle (7) is communicated with base oil import (1) by pipeline, the top of described blending kettle (7) is also provided with agitator three (14), the bottom of described blending kettle (7) is provided with discharge port, described discharge port is communicated with by the entrance of pipe-and-filter (9), the outlet of described strainer (9) is communicated with by the top of pipeline with degassing vessel (8), described compressed air inlet (4) is communicated with by the entrance of pipeline with described discharge port and described strainer (9), the pipeline that the top of described degassing vessel (8) is also provided with blow-down pipe (17) and is communicated with vacuum pumping opening (10), the outer setting of described degassing vessel (8) has heating cavities, the side of described heating cavities is communicated with heat conductive oil inlet (2) by pipeline, the opposite side of described heating cavities is imported and exported (3) by pipeline with thermal oil and is communicated with, the bottom of described degassing vessel (8) is communicated with product outlet (5) after pump two (18) by pipeline, described compressed air inlet (4) is communicated with the entrance of described pump two (18) and the bottom of described degassing vessel (8) by pipeline.
2. the production system of a kind of lithium soap grease according to claim 1, is characterized in that, the bottom of described saponification still (6) is also provided with agitator two (13).
3. the production system of a kind of lithium soap grease according to claim 1, it is characterized in that, pipeline between the heated chamber of described saponification still (6) and described heat conductive oil inlet (2) is two pipelines arranged side by side, and the heated chamber of described saponification still (6) and the described thermal oil pipeline imported and exported between (3) are two pipelines arranged side by side.
4. the production system of a kind of lithium soap grease according to claim 1, is characterized in that, described blending kettle (7) bottom is also provided with discharge port for subsequent use.
5. the production system of a kind of lithium soap grease according to claim 1, is characterized in that, the top of described degassing vessel (8) is provided with agitator four (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520826302.4U CN205035338U (en) | 2015-10-21 | 2015-10-21 | Lithium soap base grease production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520826302.4U CN205035338U (en) | 2015-10-21 | 2015-10-21 | Lithium soap base grease production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205035338U true CN205035338U (en) | 2016-02-17 |
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ID=55294250
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520826302.4U Expired - Fee Related CN205035338U (en) | 2015-10-21 | 2015-10-21 | Lithium soap base grease production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205035338U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110643419A (en) * | 2019-10-22 | 2020-01-03 | 新疆福克油品股份有限公司 | Saponification system and saponification method |
-
2015
- 2015-10-21 CN CN201520826302.4U patent/CN205035338U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110643419A (en) * | 2019-10-22 | 2020-01-03 | 新疆福克油品股份有限公司 | Saponification system and saponification method |
| CN110643419B (en) * | 2019-10-22 | 2024-02-20 | 新疆福克油品股份有限公司 | Saponification system and saponification method |
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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 |
Granted publication date: 20160217 Termination date: 20171021 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |