CN206911071U - A kind of NHD solution recovery systems - Google Patents
A kind of NHD solution recovery systems Download PDFInfo
- Publication number
- CN206911071U CN206911071U CN201720851544.8U CN201720851544U CN206911071U CN 206911071 U CN206911071 U CN 206911071U CN 201720851544 U CN201720851544 U CN 201720851544U CN 206911071 U CN206911071 U CN 206911071U
- Authority
- CN
- China
- Prior art keywords
- nhd
- branch pipe
- accumulator tank
- filter
- pipe
- 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.)
- Active
Links
- 238000011084 recovery Methods 0.000 title claims abstract description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000003860 storage Methods 0.000 claims abstract description 10
- 238000000227 grinding Methods 0.000 claims abstract description 9
- 230000014759 maintenance of location Effects 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 14
- 239000002351 wastewater Substances 0.000 abstract description 11
- 239000010865 sewage Substances 0.000 abstract description 8
- 208000021320 Nasu-Hakola disease Diseases 0.000 description 38
- 208000031334 polycystic lipomembranous osteodysplasia with sclerosing leukoencephaly Diseases 0.000 description 38
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of NHD solution recovery systems, and it includes trench, accumulator tank, recovery pump, filter and NHD storage tanks, the trench connected with accumulator tank is provided with below heat exchanger；The water inlet of recovery pump inside accumulator tank with connecting, the delivery port of recovery pump connects with the first branch pipe of three-way pipe, second branch pipe of three-way pipe is connected with the water inlet of coal-grinding tank, and the 3rd branch pipe of three-way pipe connects with the water inlet of filter, and the delivery port of filter is connected by pipeline with NHD storage tanks.Advantage：The NHD that heat exchanger is revealed is recycled, improves NHD utilization rates, reduces production cost, meanwhile, prevent NHD from entering sewage disposal pipe network, and then ensure the treatment effect of sewage disposal system；In addition, being collected in daily production using the application to producing waste water caused by system as coal-grinding water, water resources consumption is reduced.
Description
Technical field：
NHD solution recovery technologies field is the utility model is related to, relates in particular to a kind of NHD solution recovery systems.
Background technology：
Removing hydrogen sulfide, the sour gas such as carbon dioxide purification process in, on the one hand, need using NHD solution come
Sour gas is absorbed, the NHD solution for absorbing sour gas is changed into rich solution；On the other hand, need high temperature NHD lean solutions again (not
Absorb sour gas NHD solution) and NHD rich solutions be passed through plate type heat exchanger and exchanged heat；But NHD lean solutions and rich solution are in plate
The risk of NHD solution leakage occurs in formula heat exchanger in heat transfer process, causes NHD solution losses to increase, increases production cost；
Also, once reveal, NHD solution will be directly entered the sewage disposal pipe network of plant area, still, because NHD solvents belong to
Long carbon chain organic matter, existing sewage disposal system can not be handled NHD solvents, and then NHD solution is mixed into sewage network meeting
Directly affect the effect of sewage disposal.
Utility model content：
The purpose of this utility model is to provide a kind of NHD solution recovery systems for solving problem described in background technology.
The utility model is implemented by following technical scheme：A kind of NHD solution recovery systems, it includes trench, accumulator tank, returned
Pump, filter and NHD storage tanks are received, the trench connected with the accumulator tank is provided with below heat exchanger；The recovery
With being connected inside the accumulator tank, the delivery port of the recovery pump connects the water inlet of pump with the first branch pipe of three-way pipe, described
Second branch pipe of three-way pipe connects with the water inlet of coal-grinding tank, the 3rd branch pipe of the three-way pipe and the water inlet of the filter
Mouth connection, the delivery port of the filter are connected by pipeline with the NHD storage tanks；The first control is equiped with the second branch pipe
Valve, the second control valve is equiped with the 3rd branch pipe, is equiped with and leads on second branch pipe and the 3rd branch pipe
Drench valve.
Further, the recovery pump is submerged pump.
Further, the trench is obliquely installed from high to low from the heat exchanger to the accumulator tank.
The advantages of the utility model：The NHD that heat exchanger is revealed is recycled, improves NHD utilization rates, is reduced
Production cost, meanwhile, prevent NHD from entering sewage disposal pipe network, and then ensure the treatment effect of sewage disposal system；In addition,
It is collected in daily production using the application to producing waste water caused by system as coal-grinding water, reduces water resources consumption.
Brief description of the drawings：
Fig. 1 is overall structure diagram of the present utility model.
Trench 1, accumulator tank 2, recovery pump 3, filter 4, NHD storage tanks 5, heat exchanger 6, three-way pipe 7, the first branch pipe 7.1,
Two branch pipes 7.2, coal-grinding tank 8, the 3rd branch pipe 7.3, the first control valve 9, the second control valve 10, showering guilding valve 11.
Embodiment：
As shown in figure 1, a kind of NHD solution recovery systems, it includes trench 1, accumulator tank 2, recovery pump 3, the and of filter 4
NHD storage tanks 5, are provided with the trench 1 connected with accumulator tank 2 in the lower section of heat exchanger 6, trench 1 from heat exchanger 6 to accumulator tank 2 by
High to be set to low dip, the NHD solution or rainwater revealed by heat exchanger 6 can be directly after trenches 1, and edge lands under gravity
Ditch 1 is flowed into accumulator tank 2；Recovery pump 3 is submerged pump, and the water inlet of recovery pump 3 connects with the inside of accumulator tank 2, and recovery pump 3 can incite somebody to action
Solution in accumulator tank 2 pumps out；The delivery port of recovery pump 3 connects with the first branch pipe 7.1 of three-way pipe 7, second of three-way pipe 7
Pipe 7.2 connects with the water inlet of coal-grinding tank 8, and the 3rd branch pipe 7.3 of three-way pipe 7 connects with the water inlet of filter 4, filter
4 delivery port is connected by pipeline with NHD storage tanks 5；The first control valve 9 is equiped with the second branch pipe 7.2, in the 3rd branch pipe
The second control valve 10 is equiped with 7.3, showering guilding valve 11 is equiped with the second branch pipe 7.2 and the 3rd branch pipe 7.3.
Operation instruction：In daily production, the first control valve 9, the second control valve 10, recovery pump 3 and showering guilding valve 11 are closed,
Waste pipe caused by system production is placed in trench 1, and opens the draining valve on waste pipe, production waste water is entered trench 1,
And imported through trench 1 in accumulator tank 2, when the production waste water in accumulator tank 2 reaches certain liquid level, the first control valve 9 is opened, and
Start recovery pump 3, the production waste water collected in accumulator tank 2 is pumped into coal-grinding tank 8 by recovery pump 3 is used as coal-grinding water；
When solution NHD solution leakage accident occurs in heat exchanger 6, by waste pipe caused by the first control valve 9, system production
On draining valve close, open the showering guilding valve 11 on the first branch pipe 7.1, make recovery pump 3 by the production waste water in accumulator tank 2 by the
Showering guilding valve 11 on one branch pipe 7.1 is discharged, and detects NHD concentration in the waste water of the showering guilding valve 11 discharge in real time, when detecting NHD
Concentration with add heat exchanger 6 NHD solution concentration it is identical when, illustrate no longer to contain waste water in accumulator tank 2, close this and lead leaching
Valve 11, and the second control valve 10 is opened, the NHD solution collected in accumulator tank 2 is pumped into filter 4 by recovery pump 3, and filter 4 can
The impurity in NHD solution is filtered out, the NHD solution after filtering, which is entered in NHD storage tanks 5, to be reclaimed, to recycle；
When the maintenance of heat exchanger 6 terminates no longer to reveal solution, the second control valve 10 is closed, opens draining valve and the 3rd branch pipe
Showering guilding valve 11 on 7.3, now waste water caused by production continue on through trench 1 and enter accumulator tank 2, recovery pump 3 is by accumulator tank 2
Interior waste water is pumped into after the 3rd branch pipe 7.3 with NHD solution and discharged through showering guilding valve 11, and detects the molten of the showering guilding valve 11 discharge in real time
NHD concentration in liquid, when can't detect NHD solution, illustrating all production waste water in accumulator tank 2, now closing this and lead leaching
Valve 11 opens the first control valve 9.
Preferred embodiment of the present utility model is these are only, it is all in this practicality not to limit the utility model
Within new spirit and principle, any modification, equivalent substitution and improvements made etc., guarantor of the present utility model should be included in
Within the scope of shield.
Claims (3)
1. a kind of NHD solution recovery systems, it is characterised in that it includes trench, accumulator tank, recovery pump, filter and NHD storages
Groove, the trench connected with the accumulator tank is provided with below heat exchanger；The water inlet of the recovery pump with described time
Receive and connected inside groove, the delivery port of the recovery pump connect with the first branch pipe of three-way pipe, the second branch pipe of the three-way pipe and
The water inlet connection of coal-grinding tank, the 3rd branch pipe of the three-way pipe connect with the water inlet of the filter, the filter
Delivery port connected by pipeline with the NHD storage tanks；The first control valve is equiped with second branch pipe, the described 3rd
The second control valve is equiped with branch pipe, showering guilding valve is equiped with second branch pipe and the 3rd branch pipe.
2. a kind of NHD solution recovery systems according to claim 1, it is characterised in that the recovery pump is submerged pump.
3. according to a kind of any described NHD solution recovery systems of claim 1 or 2, it is characterised in that the trench is by described
Heat exchanger is obliquely installed from high to low to the accumulator tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720851544.8U CN206911071U (en) | 2017-07-13 | 2017-07-13 | A kind of NHD solution recovery systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720851544.8U CN206911071U (en) | 2017-07-13 | 2017-07-13 | A kind of NHD solution recovery systems |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206911071U true CN206911071U (en) | 2018-01-23 |
Family
ID=61348549
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720851544.8U Active CN206911071U (en) | 2017-07-13 | 2017-07-13 | A kind of NHD solution recovery systems |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206911071U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109675363A (en) * | 2018-12-26 | 2019-04-26 | 南通正拓气体有限公司 | Novel NHD solution purification process |
-
2017
- 2017-07-13 CN CN201720851544.8U patent/CN206911071U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109675363A (en) * | 2018-12-26 | 2019-04-26 | 南通正拓气体有限公司 | Novel NHD solution purification process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206911071U (en) | A kind of NHD solution recovery systems | |
| CN204661330U (en) | A kind of phosphoric acid recovery system of formed aluminum foil production line | |
| CN205555129U (en) | Oil tank oil spilling processing system | |
| CN203521553U (en) | Acidic liquid recycling device for external formation of lead storage battery | |
| CN202545290U (en) | Liquid ring vacuum pump closed loop system | |
| CN203507823U (en) | Online restoring immersion ultrafiltration membrane pool for pumping water | |
| CN202089815U (en) | Sewage treatment device | |
| CN206396856U (en) | A kind of roof rain water collecting treatment for reuse system | |
| CN103711687A (en) | Sewage recycling and automatic disposal device | |
| CN201333372Y (en) | Tail gas recovery device of methanol tower | |
| CN206956038U (en) | A kind of biogas fermentation device of positive/negative-pressure protection | |
| CN205876273U (en) | A water injection structure for low permeability pay horizontal well | |
| CN223375587U (en) | An emergency transfer facility for hazardous chemicals in shale gas produced water | |
| CN105888632B (en) | A kind of flushing device | |
| CN205838597U (en) | Nitrogen fertilizer plant's fertilizer heap penetrant collects recovery system | |
| CN213450355U (en) | Automatic medicine adding device | |
| CN103285733A (en) | Two-way utilization method and device for wet process circulation desulfurization recovered solution | |
| CN205778781U (en) | A kind of pressure waterpower surging injector | |
| CN108245919A (en) | A kind of device for continuously recycling and recovery method of the dichloromethane containing chlorine | |
| CN202209895U (en) | Steam-water mixing device for recycling heat of slag stewing steam | |
| CN102259968B (en) | Sewage treatment device and sewage treatment method using same | |
| CN206174102U (en) | Safe diverging device and use its rainwater recovery system and sewage return -flow system | |
| CN210886112U (en) | Annealing stove sealing water recovery unit | |
| CN202638393U (en) | MDI (diphenyl-methane-diisocyanate) melting system | |
| CN104864765A (en) | Vacuum water-feeding system of cooling tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |