CN205412334U - Be applied to carbon black production's raw oil oil -water separator - Google Patents
Be applied to carbon black production's raw oil oil -water separator Download PDFInfo
- Publication number
- CN205412334U CN205412334U CN201620103684.2U CN201620103684U CN205412334U CN 205412334 U CN205412334 U CN 205412334U CN 201620103684 U CN201620103684 U CN 201620103684U CN 205412334 U CN205412334 U CN 205412334U
- Authority
- CN
- China
- Prior art keywords
- waste water
- raw oil
- carbon black
- water reservoir
- oil
- 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
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 239000006229 carbon black Substances 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 16
- 239000002351 wastewater Substances 0.000 claims abstract description 43
- 238000009835 boiling Methods 0.000 claims description 11
- 239000008235 industrial water Substances 0.000 claims description 10
- 238000000926 separation method Methods 0.000 claims description 6
- 239000002912 waste gas Substances 0.000 abstract description 6
- 230000018044 dehydration Effects 0.000 abstract description 4
- 238000006297 dehydration reaction Methods 0.000 abstract description 4
- 229930195733 hydrocarbon Natural products 0.000 abstract description 2
- 150000002430 hydrocarbons Chemical class 0.000 abstract description 2
- 238000000034 method Methods 0.000 abstract description 2
- 239000000498 cooling water Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 230000001681 protective effect Effects 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 35
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000005587 bubbling Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model provides a be applied to carbon black production's raw oil oil -water separator, raw oil storage tank (1) inner chamber lower extreme is equipped with heating steam pipe (5), from the top down is equipped with a plurality of play water pipe valve (2) in proper order on the outer wall of raw oil storage tank (1) upper end, the utility model discloses a raw oil dehydration process is pollution -free, a small amount of recovering of vaporized hydrocarbons to the environment, and waste water is used for carbon black production rapid cooling water, reaches the zero release of waste water waste gas, need not other environmentally protective facility and drops into, because raw oil preheating temperature is low, light oil most in the raw oil can not volatilize, need not any running equipment, and production easy operation is energy -concerving and environment -protective.
Description
Technical field
This utility model relates to a kind of segregation apparatus, particularly relates to a kind of raw oil oily-water seperating equipment being applied to production of carbon black.
Background technology
Raw oil is the primary raw material of production of carbon black, the raw oil that buying comes all contains certain moisture, and raw oil moisture has important impact to product quality, the yield of white carbon black, in general, raw oil moisture just can put into the production of white carbon black less than 1%, so raw oil must be carried out processed before putting into production of carbon black.
The dehydrating operations of raw oil in the past, it is that the raw oil steam in drain sump is heated to about 100 DEG C, bubbling dehydration is carried out again with roots blower, moisture in raw oil becomes water vapour and discharges with air, containing harmful substance in the waste gas discharged, outer row can cause atmospheric pollution, and processes these waste gas enterprise operation to be increased cost.
Summary of the invention
The purpose of this utility model is to provide a kind of raw oil oily-water seperating equipment being applied to production of carbon black, when solving the dehydration of existing raw oil, moisture in raw oil becomes water vapour and discharges with air, containing harmful substance in the waste gas discharged, outer row can cause atmospheric pollution, and the problem processing these waste gas enterprise operation to be increased cost.
This utility model is realized in, it includes raw oil storage tank, outlet pipe valve, reception funnel, waste water connecting tube, add live steam pipe, waste water reservoir one, waste water reservoir two, light boiling point oil export, industrial water exports, dividing plate, it is characterized in that, described raw oil storage tank inner chamber lower end is provided with and adds live steam pipe, several outlet pipe valves it are sequentially provided with from top to bottom on the outer wall of described raw oil storage tank upper end, described outlet pipe valve connects waste water connecting tube by reception funnel, described waste water connecting tube connects the lower end of waste water reservoir one, side, described waste water reservoir one upper end is provided with light boiling point oil export, described waste water reservoir one connects waste water reservoir two by vertical dividing plate, described dividing plate is 30mm with the vertical dimension of the bottom of waste water reservoir two, upper end, described waste water reservoir two side is provided with industrial water outlet.
Perpendicular separation between described outlet pipe valve is adjacent is 5 10cm.
Lateral separation between described outlet pipe valve is adjacent is 5 10cm.
The height of described industrial water outlet is less than the height 30mm of light boiling point oil export.
Of the present utility model have the technical effect that this utility model achieves pollution-free to environment of raw oil dehydration, a small amount of recovering of vaporized hydrocarbons, waste water is used for production of carbon black chilling water, reach the zero-emission of waste water and gas, it is not necessary to other environmental protection facilities put into, owing to fuel oil preheating temperature is low, in raw oil, most light oil will not volatilize, without any running device, production operation is simple, energy-conserving and environment-protective.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In the drawings, 1, raw oil storage tank 2, outlet pipe valve 3, reception funnel 4, waste water connecting tube 5, add live steam pipe 6, waste water reservoir 1, waste water reservoir 28, light boiling point oil export 9, industrial water outlet 10, dividing plate.
Detailed description of the invention
This utility model is illustrated in conjunction with Fig. 1, described raw oil storage tank (1) inner chamber lower end is provided with and adds live steam pipe (5), several outlet pipe valves (2) it are sequentially provided with from top to bottom on the outer wall of described raw oil storage tank (1) upper end, described outlet pipe valve (2) connects waste water connecting tube (4) by reception funnel (3), described waste water connecting tube (4) connects the lower end of waste water reservoir one (6), described waste water reservoir one (6) side, upper end is provided with light boiling point oil export (8), described waste water reservoir one (6) connects waste water reservoir two (7) by vertical dividing plate (10), described dividing plate (10) is 30mm with the vertical dimension of the bottom of waste water reservoir two (7), described waste water reservoir two (7) upper end, side is provided with industrial water outlet (9).
Perpendicular separation between described outlet pipe valve (2) is adjacent is 5 10cm.
Lateral separation between described outlet pipe valve (2) is adjacent is 5 10cm.
The height of described industrial water outlet (9) is less than the height 30mm of light boiling point oil export (8).
During work, raw oil entrance raw oil storage tank (1) is opened afterwards and is added live steam pipe (5), to close after fuel oil preheating to uniform temperature, by raw oil storage tank (1) static placement more than 24 hours, the proportion of water is lighter than oil just to be floated on above oil, open successively from uppermost outlet pipe valve (2), by the water on top after reception funnel (3) enters waste water connecting tube (4), enter waste water reservoir one (6), in waste water, light boiling point oil is floated on the surface of waste water reservoir one (6) by the stop of dividing plate (10), reclaimed through light boiling point oil export (8), and waste water enters waste water reservoir two (7) from dividing plate (10) underclearance, chilled water (chw) needed for industrial water outlet (9) supply reactor for production of carbon black.
Embodiment described above is only to be described preferred implementation of the present utility model; not scope of the present utility model is defined; on the premise of without departing from this utility model design spirit; various deformation that the technical solution of the utility model is made by those of ordinary skill in the art and improvement, all should fall in the protection domain that this utility model claims determine.
Claims (4)
- null1. the raw oil oily-water seperating equipment being applied to production of carbon black，It includes raw oil storage tank (1)、Outlet pipe valve (2)、Reception funnel (3)、Waste water connecting tube (4)、Add live steam pipe (5)、Waste water reservoir one (6)、Waste water reservoir two (7)、Light boiling point oil export (8)、Industrial water outlet (9)、Dividing plate (10)，It is characterized in that，Described raw oil storage tank (1) inner chamber lower end is provided with and adds live steam pipe (5)，Several outlet pipe valves (2) it are sequentially provided with from top to bottom on the outer wall of described raw oil storage tank (1) upper end，Described outlet pipe valve (2) connects waste water connecting tube (4) by reception funnel (3)，Described waste water connecting tube (4) connects the lower end of waste water reservoir one (6)，Described waste water reservoir one (6) side, upper end is provided with light boiling point oil export (8)，Described waste water reservoir one (6) connects waste water reservoir two (7) by vertical dividing plate (10)，Described dividing plate (10) is 30mm with the vertical dimension of the bottom of waste water reservoir two (7)，Described waste water reservoir two (7) upper end, side is provided with industrial water outlet (9).
- A kind of raw oil oily-water seperating equipment being applied to production of carbon black the most according to claim 1, it is characterised in that the perpendicular separation between described outlet pipe valve (2) is adjacent is 5 10cm.
- A kind of raw oil oily-water seperating equipment being applied to production of carbon black the most according to claim 1, it is characterised in that the lateral separation between described outlet pipe valve (2) is adjacent is 5 10cm.
- A kind of raw oil oily-water seperating equipment being applied to production of carbon black the most according to claim 1, it is characterised in that the height of described industrial water outlet (9) is less than the height 30mm of light boiling point oil export (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620103684.2U CN205412334U (en) | 2016-02-02 | 2016-02-02 | Be applied to carbon black production's raw oil oil -water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620103684.2U CN205412334U (en) | 2016-02-02 | 2016-02-02 | Be applied to carbon black production's raw oil oil -water separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205412334U true CN205412334U (en) | 2016-08-03 |
Family
ID=56540477
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620103684.2U Expired - Fee Related CN205412334U (en) | 2016-02-02 | 2016-02-02 | Be applied to carbon black production's raw oil oil -water separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205412334U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775833A (en) * | 2019-02-28 | 2019-05-21 | 唐山黑猫炭黑有限责任公司 | The processing unit and method of the bright water of tar in a kind of carbon black generating process |
-
2016
- 2016-02-02 CN CN201620103684.2U patent/CN205412334U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775833A (en) * | 2019-02-28 | 2019-05-21 | 唐山黑猫炭黑有限责任公司 | The processing unit and method of the bright water of tar in a kind of carbon black generating process |
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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: 20160803 |