CN205953572U - Methyl alcohol / separation of water tower wastewater discharge system - Google Patents
Methyl alcohol / separation of water tower wastewater discharge system Download PDFInfo
- Publication number
- CN205953572U CN205953572U CN201620994756.7U CN201620994756U CN205953572U CN 205953572 U CN205953572 U CN 205953572U CN 201620994756 U CN201620994756 U CN 201620994756U CN 205953572 U CN205953572 U CN 205953572U
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- CN
- China
- Prior art keywords
- stop valve
- methanol
- water
- knockout tower
- level control
- 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
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Abstract
The utility model discloses a methyl alcohol / separation of water tower wastewater discharge system, including methyl alcohol / separation of water tower, be provided with useless water chiller on methyl alcohol / separation of water tower waste water drain line, still be provided with the fluid level control valve between useless water chiller and the wastewater discharge export, still be provided with stop valve A between methyl alcohol / separation of water tower and the useless water chiller, still be connected with stop valve B's wherein one end between stop valve A and the useless water chiller, stop valve B and the parallelly connected stop valve C that is provided with in the both ends of methyl alcohol / separation of water tower waste water drain line connection point, still be provided with stop valve D between useless water chiller and the fluid level control valve, stop valve E and stop valve F has still set gradually between fluid level control valve and the wastewater discharge export, still be connected with stop valve H's wherein one end between fluid level control valve and the stop valve E, the utility model provides a have the liquid hammer phenomenon that exists at slurry pressure gasification preparation methyl alcohol in -process now to lead to equipment to damage serious, problem that cost of maintenance is high.
Description
Technical field
This utility model belongs to coal slurry pressurized gasification to be prepared methanol technics low-temp methanol and washes technical field and in particular to a kind of
Methanol/water knockout tower waste water drainage system.
Background technology
In coal slurry pressurized gasification preparation methanol process, conversion gas carry a large amount of saturation waters and enter rectisol system,
Wherein most enters methanol/water knockout tower after catching through spray methanol.Meanwhile, the washess of tail gas washing tower, first
The part High water cut methanol solution of alcohol regenerator right ventricle, and quantitative alkali liquor (concentration known) is also sent to methanol/water in the lump and divides
From tower, realize efficiently separating of methanol and water, final water and catalyst fines and other impurities in the form of the waste water outside drain into after
Sequence biochemical treatment unit.So, the quality that methanol/water knockout tower operating mode is run will directly influence the product of system circulation methanol
Matter, and determine bottom of towe waste water whether can qualified discharge.
Methanol/water knockout tower discharge of wastewater pipeline is provided with a U-tube formula water cooler E7620, and wherein waste water is walked shell side, followed
Ring water walks tube side, to reduce the temperature sending waste water outside, simultaneously for more easily controlling the liquid level of methanol/water knockout tower, safeguards tower
Interior operating condition, is mounted with remote liquid level control valve LV7619, and before being in E7620 shell side inlet.
In system during normal operation, typically at 141 DEG C about, pressure can for the temperature of methanol/water separation tower bottom waste water
Reach more than 0.25MPa (G).When the operating load of methanol/water knockout tower is relatively low, and LV7619 aperture is less, E7620 will appear from
Significantly liquid hit phenomenon, especially at its shell side inlet, performance is even more serious.Nearly 3 years, using maintenance when to E7620 manage
Bundle implements four plugging operation, but its damaged condition of later stage is excessive, can not meet the requirement of normal process conditions completely, in
Be by integral replacing, this not only adds additional the operating cost of device, and have impact on system " peace, steady, long, full,
Excellent " running environment.Analysis reason, mainly due to methanol/water knockout tower hot waste water through LV7619 throttling, after blood pressure lowering,
Part vaporizes, therefore is carrying out, in heat transfer process, leading to E7620 liquid hit phenomenon with E7620 tube side recirculated water.
Utility model content
The purpose of this utility model be provide a kind of methanol/water knockout tower waste water drainage system, solve existing in coal slurry
Present in pressurized gasification preparation methanol process, liquid hit phenomenon leads to device damage serious, the high problem of maintenance cost.
This utility model be employed technical scheme comprise that, a kind of methanol/water knockout tower waste water drainage system, including methanol/
Water separation column, methanol/water knockout tower discharge of wastewater pipeline is provided with gaseous effluent cooler, gaseous effluent cooler and discharge of wastewater outlet
Between be additionally provided with fluid level control valve.
Feature of the present utility model also resides in,
It is additionally provided with stop valve A, between stop valve A and gaseous effluent cooler between methanol/water knockout tower and gaseous effluent cooler
It is also associated with wherein one end of stop valve B, stop valve B is in parallel with the two ends of methanol/water knockout tower discharge of wastewater pipeline junction point
It is provided with shutoff valve C.
It is additionally provided with stop valve D, fluid level control valve and discharge of wastewater export it between gaseous effluent cooler and fluid level control valve
Between be also disposed with stop valve E and stop valve F, be also associated with wherein the one of stop valve G between gaseous effluent cooler and stop valve D
End, is also associated with wherein one end of stop valve H between fluid level control valve and stop valve E.
It is also associated with stop valve I between stop valve D entrance point and the port of export of stop valve E.
Fluid level control valve model LV7619.
Gaseous effluent cooler model E7620.
The beneficial effects of the utility model are that a kind of methanol/water knockout tower waste water drainage system, to methanol/water separation
After LV7619 installation site implements transformation on tower 1 discharge of wastewater pipeline, send throttling at LV7619 for the waste water outside, pressure reduction will
Occur after it carries out heat exchange with E7620 tube side recirculated water, temperature now is reduced to less than 40 DEG C, therefore inherently eliminates
There is the possibility of vaporization in waste water.
Brief description
Fig. 1 is a kind of structural representation of this utility model methanol/water knockout tower waste water drainage system.
In figure, 1. methanol/water knockout tower, 2. gaseous effluent cooler, 3. stop valve A, 4. stop valve B, 5. shutoff valve C, 6. section
Only valve G, 7. fluid level control valve, 8. stop valve D, 9. stop valve E, 10. stop valve F, 11. stop valve H, 12. stop valve I.
Specific embodiment
With reference to the accompanying drawings and detailed description this utility model is described in detail.
A kind of this utility model methanol/water knockout tower waste water drainage system, by methanol/water knockout tower discharge of wastewater pipeline
The installation site of LV7619 is transformed to shell-side outlet by before E7620 shell side inlet, and simultaneously taking account of the later stage may be to E7620 shell
The discharge opeing of Cheng Jinhang or cleaning operation, have added one before stop valve before improved LV7619 and have got rid of head, in the former peace of LV7619
Add one on the connection short tube of holding position and lead pouring, specific as follows：
A kind of methanol/water knockout tower waste water drainage system, structure as shown in figure 1, include methanol/water knockout tower 1, methanol/
Gaseous effluent cooler 2, gaseous effluent cooler 2 model E7620, gaseous effluent cooler 2 He are provided with water separation column 1 discharge of wastewater pipeline
It is additionally provided with fluid level control valve 7, fluid level control valve 7 model LV7619, methanol/water knockout tower 1 He between discharge of wastewater outlet
It is additionally provided with stop valve A3 between gaseous effluent cooler 2, between stop valve A3 and gaseous effluent cooler 2, be also associated with stop valve B4 its
Middle one end, stop valve B4 has been arranged in parallel shutoff valve C 5 with the two ends of methanol/water knockout tower 1 discharge of wastewater pipeline junction point, gives up
Be additionally provided with stop valve D8 between water cooler 2 and fluid level control valve 7, between fluid level control valve 7 and discharge of wastewater outlet also according to
Secondary be provided with stop valve E9 and stop valve F10, be also associated with wherein the one of stop valve G6 between gaseous effluent cooler 2 and stop valve D8
End, is also associated with wherein one end of stop valve H11 between described fluid level control valve 7 and stop valve E9, stop valve D8 entrance point and
It is also associated with stop valve I12 between the port of export of stop valve E9.
A kind of this utility model methanol/water knockout tower waste water drainage system, to methanol/water knockout tower 1 wastewater discharge pipe
On line LV7619 installation site implement transformation after, send throttling LV7619 at for the waste water outside, pressure reduction will occur in itself and
After E7620 tube side recirculated water carries out heat exchange, temperature now is reduced to less than 40 DEG C, therefore inherently eliminates waste water and occur
The possibility of vaporization.
A kind of this utility model methanol/water knockout tower waste water drainage system, on the one hand can thoroughly eliminate E7620 liquid hammer and ask
Topic, extends its service life, reduces the operating cost of device；On the other hand, optimize the operating condition of methanol/water knockout tower,
Can be further assured that the qualified discharge sending waste water outside, simultaneously water content in the regeneration effect to Mathanol regenerating tower and recycle methanol
Low level controls the certain facilitation of generation；3rd, the technological transformation involved by this invention is convenient to carry out, and cost of investment is relatively
Low.
Claims (6)
1. a kind of methanol/water knockout tower waste water drainage system is it is characterised in that include methanol/water knockout tower (1), methanol/water is divided
Gaseous effluent cooler (2) is provided with tower (1) discharge of wastewater pipeline, also sets between gaseous effluent cooler (2) and discharge of wastewater outlet
It is equipped with fluid level control valve (7).
2. a kind of methanol/water knockout tower waste water drainage system according to claim 1 is it is characterised in that described methanol/water
It is additionally provided with stop valve A (3), between stop valve A (3) and gaseous effluent cooler (2) between knockout tower (1) and gaseous effluent cooler (2)
It is also associated with wherein one end of stop valve B (4), described stop valve B (4) is connected with methanol/water knockout tower (1) discharge of wastewater pipeline
The two ends of point have been arranged in parallel shutoff valve C (5).
3. a kind of methanol/water knockout tower waste water drainage system according to claim 1 is it is characterised in that described waste water is cold
But it is additionally provided with stop valve D (8) between device (2) and fluid level control valve (7), between fluid level control valve (7) and discharge of wastewater outlet
Also it is disposed with stop valve E (9) and stop valve F (10), be also associated between described gaseous effluent cooler (2) and stop valve D (8)
Wherein one end of stop valve G (6), be also associated between described fluid level control valve (7) and stop valve E (9) stop valve H (11) its
Middle one end.
4. a kind of methanol/water knockout tower waste water drainage system according to claim 3 is it is characterised in that described stop valve D
(8) it is also associated with stop valve I (12) between the port of export of entrance point and stop valve E (9).
5. a kind of methanol/water knockout tower waste water drainage system according to claim 1 is it is characterised in that described liquid level control
Valve (7) model LV7619 processed.
6. a kind of methanol/water knockout tower waste water drainage system according to claim 1 is it is characterised in that described waste water is cold
But device (2) model E7620.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620994756.7U CN205953572U (en) | 2016-08-29 | 2016-08-29 | Methyl alcohol / separation of water tower wastewater discharge system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620994756.7U CN205953572U (en) | 2016-08-29 | 2016-08-29 | Methyl alcohol / separation of water tower wastewater discharge system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205953572U true CN205953572U (en) | 2017-02-15 |
Family
ID=57978883
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620994756.7U Expired - Fee Related CN205953572U (en) | 2016-08-29 | 2016-08-29 | Methyl alcohol / separation of water tower wastewater discharge system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205953572U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114432846A (en) * | 2022-01-04 | 2022-05-06 | 中国神华煤制油化工有限公司 | Drainage device and low-temperature methanol washing equipment |
-
2016
- 2016-08-29 CN CN201620994756.7U patent/CN205953572U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114432846A (en) * | 2022-01-04 | 2022-05-06 | 中国神华煤制油化工有限公司 | Drainage device and low-temperature methanol washing equipment |
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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: 20170215 Termination date: 20200829 |