CN103831035A - Mixing device of liquid neopentyl glycol - Google Patents
Mixing device of liquid neopentyl glycol Download PDFInfo
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- CN103831035A CN103831035A CN201410013895.2A CN201410013895A CN103831035A CN 103831035 A CN103831035 A CN 103831035A CN 201410013895 A CN201410013895 A CN 201410013895A CN 103831035 A CN103831035 A CN 103831035A
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- neopentyl glycol
- mixing
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- liquid
- preparing tank
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Abstract
The invention discloses a mixing device of liquid neopentyl glycol, which comprises a finished product kettle, a finished product kettle conveying pipeline, a preparation pot, and a soft water tank; liquid neopentyl glycol in the finished product kettle is conveyed to the preparation pot through a material feeding pump; the conveying amount of the liquid neopentyl glycol is controlled by a liquid flow solenoid valve disposed on the material feeding pump; a miniature mixing container is disposed in the preparation pot; the miniature mixing container is cylindrical; a mixing tank is disposed in the miniature mixing container; soft water in the soft water tank directly flows to the bottom of the mixing tank through a pipeline; liquid neopentyl glycol also extends to the middle part of the mixing tank through a pipeline; the mixed liquid neopentyl glycol flows into the preparation pot; the bottom of the preparation pot is funnel-shaped; an output pipeline is disposed at the bottom of the preparation pot; the mixed liquid neopentyl glycol is conveyed to a top input pipeline of the preparation pot through a circulating pump; circulating mixing is performed in the preparation pot for several times; and the product is conveyed to a storage tank by detection control. The mixing device of the invention is characterized in that a flow solenoid valve is disposed to control the inlet amounts of liquid neopentyl glycol and water, so as to maintain the ratio to be constant, and thus to cause no error; the mixing tank is additionally disposed in the preparation pot, so when water enters the pot at first and liquid neopentyl glycol enters the pot later, full mixing is carried out, the mixed liquid enters the preparation pot, and the requirements can be met by a few cycles.
Description
Technical field
The present invention relates to a kind of mixing arrangement of liquid neopentyl glycol.
Background technology
The configuration of liquid neopentyl glycol normally joins 10% water in preparing tank, again 90% neopentyl glycol is joined in preparing tank, with the circulating pump mixing that repeatedly circulates, the liquid neopentyl glycol mixing is sent in accumulator tank, use this way major defect to be that liquid neopentyl glycol inlet amount cannot control, amount of water is also accurate not, and incorporation time is long.
Summary of the invention
The object of the present invention is to provide a kind of inlet amount accurate, error free, mix mixing arrangement abundant and the liquid neopentyl glycol that the time is short.
Object of the present invention is achieved through the following technical solutions: the mixing arrangement of this liquid neopentyl glycol comprises finished product still, finished product still conveyance conduit, preparing tank, demineralized water tank, liquid neopentyl glycol in finished product still is transported in preparing tank by feeding pump, liquid neopentyl glycol conveying capacity is by being arranged on the fluid flow solenoid control of feeding pump, in preparing tank, be provided with small-sized mixer, small-sized mixer is column type, in small-sized mixer, be provided with mixing channel), soft water in demineralized water tank directly enters the bottom of mixing channel by pipeline, liquid neopentyl glycol also extend into mixing channel middle part by pipeline, the liquid neopentyl glycol mixing flow in preparing tank, preparing tank bottom is funnel-form, preparing tank bottom arranges output channel and by circulating pump, mixing material neopentyl glycol is delivered into the top input channel of preparing tank, mixing repeatedly circulates in preparing tank, then control and deliver into accumulator tank by detection,
Discharge magnetic valve is set on described demineralized water tank, is transported to the mixing channel in preparing tank by pipeline;
The top of described preparing tank arranges pressure-control valve.
Feature of the present invention is arranging flow solenoid valve, controls liquid neopentyl glycol and water inlet, and its proportional quantity is remained unchanged, error free; In preparing tank, increase a mixing channel, be introduced into water, in the situation of laggard liquid neopentyl glycol, fully mix, the liquid mixing enters preparing tank again and can meet the demands by a small amount of circulation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
1, finished product still 2, conveyance conduit 3, fluid flow magnetic valve 4, feeding pump 5, preparing tank 6, mixer 7, discharge magnetic valve 8, circulating pump 9, demineralized water tank 10, accumulator tank 11, mixing channel.
The specific embodiment
By reference to the accompanying drawings the utility model is described in further detail.
As can be seen from Figure 1, the mixing arrangement of this liquid neopentyl glycol comprises finished product still 1, finished product still conveyance conduit 2, preparing tank 5, demineralized water tank 9, liquid neopentyl glycol in finished product still 1 is transported in preparing tank 5 by feeding pump 4, liquid neopentyl glycol conveying capacity is controlled by the fluid flow magnetic valve 3 that is arranged on feeding pump 4, in preparing tank 5, be provided with small-sized mixer 6, small-sized mixer 6 is column type, in small-sized mixer 6, be provided with mixing channel 11, soft water in demineralized water tank 9 directly enters the bottom of mixing channel 11 by pipeline, liquid neopentyl glycol also extend into mixing channel 11 middle parts by pipeline, the liquid neopentyl glycol mixing flow in preparing tank 5, preparing tank 5 bottoms are funnel-form, preparing tank 5 bottoms arrange output channel and by circulating pump 8, mixing material neopentyl glycol are delivered into the top input channel of preparing tank 5, mixing repeatedly circulates in preparing tank 5, then control and deliver into accumulator tank 10 by detection, discharge magnetic valve 7 is set on demineralized water tank 9, be transported to the mixing channel in preparing tank 5 by pipeline, the top of preparing tank 5 arranges pressure-control valve 12.
Claims (3)
1. a mixing arrangement for liquid neopentyl glycol, comprises finished product still (1), finished product still conveyance conduit (2), preparing tank (5), demineralized water tank (9), it is characterized in that:
Liquid neopentyl glycol in finished product still (1) is transported in preparing tank (5) by feeding pump (4), liquid neopentyl glycol conveying capacity is controlled by the fluid flow magnetic valve (3) that is arranged on feeding pump (4), in preparing tank (5), be provided with small-sized mixer (6), small-sized mixer (6) is column type, in small-sized mixer (6), be provided with mixing channel (11), soft water in demineralized water tank (9) directly enters the bottom of mixing channel (11) by pipeline, liquid neopentyl glycol also extend into mixing channel (11) middle part by pipeline, the liquid neopentyl glycol mixing flow in preparing tank (5), preparing tank (5) bottom is funnel-form, preparing tank (5) bottom arranges output channel and by circulating pump (8), mixing material neopentyl glycol is delivered into the top input channel of preparing tank (5), mixing repeatedly circulates in preparing tank (5), then control and deliver into accumulator tank (10) by detection.
2. the mixing arrangement of a kind of liquid neopentyl glycol according to claim 1, is characterized in that:
Discharge magnetic valve (7) is set on demineralized water tank (9), is transported to the mixing channel in preparing tank (5) by pipeline.
3. the mixing arrangement of a kind of liquid neopentyl glycol according to claim 1, is characterized in that:
The top of preparing tank (5) arranges pressure-control valve (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410013895.2A CN103831035A (en) | 2014-01-14 | 2014-01-14 | Mixing device of liquid neopentyl glycol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410013895.2A CN103831035A (en) | 2014-01-14 | 2014-01-14 | Mixing device of liquid neopentyl glycol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103831035A true CN103831035A (en) | 2014-06-04 |
Family
ID=50795119
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410013895.2A Pending CN103831035A (en) | 2014-01-14 | 2014-01-14 | Mixing device of liquid neopentyl glycol |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103831035A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112058199A (en) * | 2020-08-25 | 2020-12-11 | 福建天甫电子材料有限公司 | Preparation system and process of electronic-grade ammonia fluoride |
-
2014
- 2014-01-14 CN CN201410013895.2A patent/CN103831035A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112058199A (en) * | 2020-08-25 | 2020-12-11 | 福建天甫电子材料有限公司 | Preparation system and process of electronic-grade ammonia fluoride |
| CN112058199B (en) * | 2020-08-25 | 2022-02-11 | 福建天甫电子材料有限公司 | Preparation system and process of electronic-grade ammonia fluoride |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20140604 |
|
| WD01 | Invention patent application deemed withdrawn after publication |