CN205973778U - Discharging equipment is changed to raffinate for gas synthesis - Google Patents
Discharging equipment is changed to raffinate for gas synthesis Download PDFInfo
- Publication number
- CN205973778U CN205973778U CN201620992127.0U CN201620992127U CN205973778U CN 205973778 U CN205973778 U CN 205973778U CN 201620992127 U CN201620992127 U CN 201620992127U CN 205973778 U CN205973778 U CN 205973778U
- Authority
- CN
- China
- Prior art keywords
- raffinate
- residual liquid
- jar
- retort
- gas
- 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
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The utility model provides a discharging equipment is changed to raffinate for gas synthesis, includes retort, first raffinate jar and second raffinate jar, the retort is connected with first raffinate jar through first motorised valve, and the retort is passed through the second motorised valve and is connected with second raffinate jar, the upper portion of retort, first raffinate jar and second raffinate jar all is provided with the gas outlet, the gas outlet of retort, first raffinate jar and second raffinate jar all with total union coupling of giving vent to anger, the bottom of first raffinate jar and second raffinate jar all is provided with the leakage fluid dram. Raffinate in the retort reaches when setting for the liquid level, and the raffinate gets into first raffinate jar, reaches when first raffinate jar is interior sets for the liquid level, and the raffinate stream is to second raffinate jar. The raffinate stops a period in first raffinate jar and first raffinate jar, and gas fully spills over, gets into the house steward that gives vent to anger by its gas outlet and discharges, and last raffinate is discharged by the leakage fluid dram. Through making the raffinate get into two raffinate jars in turn, release incomplete existing gas body back and discharge, guaranteed the continuous safe operation of gas synthesis reaction.
Description
Technical field
This utility model is related to a kind of dress for carrying out residual liquid discharge during gas being synthesized with liquid charging stock
Put, belong to chlorine dioxide generation technique field.
Background technology
It is known that some gas liquid charging stocks are synthesized, such as chlorine dioxide is usually to adopt hydrochloric acid and chlorine
Sour sodium (or sodium chlorite) is quantitatively injected in retort, and retort occurs chemical reaction to generate titanium dioxide in case of heating
Chlorine and chlorine, reacted residual liquid typically directly discharges.
But, sometimes still containing certain density gas in residual liquid, if directly discharged, that is, wasting raw material and dangerous
Property.So that the gas in residual liquid is fully discharged and make full use of, be urgently to be resolved hurrily asking during current gas synthesis
Topic.
Utility model content
This utility model is directed to the residual liquid discharge problem that existing gas synthesis technology exists, and provides one kind that residual liquid can be made to pacify
The gas synthesis residual liquid of full discharge changes tapping equipment.
Gas synthesis residual liquid of the present utility model changes tapping equipment, employs the following technical solutions：
This device, including retort, the first residual liquid tank and the second residual liquid tank；It is residual with first that retort passes through the first electrodynamic valve
Flow container connects, and retort is connected with the second residual liquid tank by the second electrodynamic valve；Retort, the first residual liquid tank and the second residual liquid tank
Top is provided with gas outlet, and the gas outlet of retort, the first residual liquid tank and the second residual liquid tank is all connected with the house steward that gives vent to anger；First
The bottom of residual liquid tank and the second residual liquid tank is provided with leakage fluid dram.
It is provided with agitating device, so that gas fully discharges in it in retort, the first residual liquid tank and the second residual liquid tank.Should
Agitating device can adopt gas mixing pipe.
It is provided with liquidometer in first residual liquid tank and the second residual liquid tank.
Feed liquid enters and chemical reaction occurs in retort, and moment produces a large amount of gases, and most of gas is by retort
Gas outlet is discharged, and a small amount of gas remains in residual liquid.When the residual liquid in retort reaches setting liquid level, the first electrodynamic valve is opened
Open, the second electrodynamic valve cuts out, residual liquid enters the first residual liquid tank, when reaching setting liquid level in the first residual liquid tank, close first electronic
Valve, opens the second electrodynamic valve, and residual liquid flows to the second residual liquid tank.When residual liquid stops one section in the first residual liquid tank and the first residual liquid tank
Between, gas fully overflows, and is entered the house steward that gives vent to anger by its gas outlet and discharges, last residual liquid is discharged by leakage fluid dram.Retort produces
Residual liquid alternately enters in two residual liquid tanks, discharges after release survival gas.
This utility model structure is simple, alternately enters two residual liquid tanks by making residual liquid, discharges, carry after release survival gas
High gas production, has saved raw material it is achieved that safety dumping is it is ensured that the continuous safe operation of gas synthesis reaction.
Brief description
Fig. 1 is the principle schematic diagram. that gas synthesis residual liquid of the present utility model changes tapping equipment.
Wherein：1st, gas outlet, 2, retort, the 3, first electrodynamic valve, the 4, second electrodynamic valve, the 5, first residual liquid tank, 6, second
Residual liquid tank, the 7, second drain valve, the 8, second gas mixing pipe, 9, second liquid level gauge, the 10, first drain valve, the 11, first gas mixing pipe, 12,
First liquid level gauge, 13, charging aperture, the 14, first leakage fluid dram, the 15, second leakage fluid dram, the 16, first gas outlet, the 17, second gas outlet,
18th, give vent to anger house steward, 19, reaction gas mixing pipe.
Specific embodiment
As shown in figure 1, gas synthesis residual liquid conversion tapping equipment of the present utility model mainly include retort 2, the
One residual liquid tank 5 and the second residual liquid tank 6.Charging aperture 13 and gas outlet 1 are provided with retort 2.Retort 2 passes through the first electrodynamic valve
3 are connected with the first residual liquid tank 5, and retort 2 is connected with the second residual liquid tank 6 by the second electrodynamic valve 4.The top of the first residual liquid tank 5
It is provided with the first gas outlet 16, the top of the second residual liquid tank 6 is provided with the second gas outlet 17.Gas outlet 1, the first gas outlet 16 and
Second gas outlet 17 is all connected with the house steward 18 that gives vent to anger.It is provided with first liquid level gauge 12, in the second residual liquid tank 6 in first residual liquid tank 5
It is provided with second liquid level gauge 9.First residual liquid tank 5 bottom is provided with the first leakage fluid dram 14, is provided with second row in the second residual liquid tank 6
Liquid mouth 15.First drain valve 10 is provided with the first leakage fluid dram 14, in the second residual liquid tank 6, is provided with setting on the second leakage fluid dram 15
There is the second drain valve 7.
In order that gas fully overflows, in retort 2, interior being provided with reacts gas mixing pipe 19, setting in the first residual liquid tank 5
There is the first gas mixing pipe 11.It is provided with the second gas mixing pipe 8 in the second residual liquid tank 6.In first residual liquid tank 5 and the second residual liquid tank 6
Other types of agitating device can be installed.
Feed liquid is entered in retort 1 by charging aperture 13, and chemical reaction occurs, and moment produces a large amount of gases, most of gas
The house steward 18 that gives vent to anger is entered by gas outlet 1, a small amount of gas retains in reacted residual liquid.Residual liquid reaches in retort 1 and sets
Liquid level when, open the first electrodynamic valve 3, close the second electrodynamic valve 4, residual liquid enter the first residual liquid tank 5, work as first liquid level gauge
When 12 liquid levels detecting in the first residual liquid tank 5 reach the high level horizontal plane setting, close the first electrodynamic valve 3, open second
Electrodynamic valve 4, residual liquid flows to the second residual liquid tank 6 by the second electrodynamic valve 4.Residual liquid stays for some time the (time in the first residual liquid tank 5
Can set as the case may be), gas mixing is carried out to the residual liquid in the first residual liquid tank 5 by the first gas mixing pipe 11, makes to retain in residual
Gas in liquid fully overflows, and enters, by first row QI KOU 12, the house steward 18 that gives vent to anger.After stirring certain time, open the first drain valve
10, residual liquid is discharged by the first leakage fluid dram 14.Enter with the first residual liquid tank 5 and the second residual liquid tank 6 before liquid material reaction in retort 1
Before liquid, reaction gas mixing pipe 19, the first gas mixing pipe 11 and the second gas mixing pipe 8 are first passed through compressed air.
Enter the same time delay of residual liquid of the second residual liquid tank 6 for a period of time, by the second gas mixing pipe 8 in the second residual liquid tank 6
Residual night carry out gas mixing, make to retain gas and fully overflow, the house steward that gives vent to anger is entered by the second exhaust port 9 on the second residual liquid tank 6 top
18, residual liquid is discharged by the second leakage fluid dram 15.
Residual liquid alternately enters the first residual liquid tank 5 and the second residual liquid tank 6 by said process, and discharges residual in two residual liquid tanks
Discharge after trapped air body.
Claims (4)
1. a kind of gas synthesis residual liquid changes tapping equipment, including retort, the first residual liquid tank and the second residual liquid tank；Its feature
It is：Retort is connected with the first residual liquid tank by the first electrodynamic valve, and retort is connected with the second residual liquid tank by the second electrodynamic valve；
The top of retort, the first residual liquid tank and the second residual liquid tank is provided with gas outlet, retort, the first residual liquid tank and the second residual liquid
The gas outlet of tank is all connected with the house steward that gives vent to anger；The bottom of the first residual liquid tank and the second residual liquid tank is provided with leakage fluid dram.
2. gas synthesis residual liquid according to claim 1 changes tapping equipment, it is characterized in that：Described retort, first
It is provided with agitating device in residual liquid tank and the second residual liquid tank.
3. gas synthesis residual liquid according to claim 2 changes tapping equipment, it is characterized in that：Described agitating device adopts
Gas mixing pipe.
4. gas synthesis residual liquid according to claim 1 changes tapping equipment, it is characterized in that：Described first residual liquid tank and
It is provided with liquidometer in second residual liquid tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620992127.0U CN205973778U (en) | 2016-08-30 | 2016-08-30 | Discharging equipment is changed to raffinate for gas synthesis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620992127.0U CN205973778U (en) | 2016-08-30 | 2016-08-30 | Discharging equipment is changed to raffinate for gas synthesis |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205973778U true CN205973778U (en) | 2017-02-22 |
Family
ID=58041354
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620992127.0U Active CN205973778U (en) | 2016-08-30 | 2016-08-30 | Discharging equipment is changed to raffinate for gas synthesis |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205973778U (en) |
-
2016
- 2016-08-30 CN CN201620992127.0U patent/CN205973778U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105967315B (en) | A kind of high-efficiency and continuous processing high ammonia-nitrogen wastewater device and its processing method | |
| CN203959058U (en) | The nitrogen envelope of volatile organism material storage tank and water seal interlock mothballed plant | |
| CN107930372A (en) | A kind of integrated device and methods for using them based on triazine solution desulfurization | |
| CN205973778U (en) | Discharging equipment is changed to raffinate for gas synthesis | |
| CN205634876U (en) | Prevent scalding, safety, low pressure, environmental protection hydrogen machine | |
| CN210279095U (en) | Spiral stirring and feeding device for producing dimethomorph | |
| CN107913535A (en) | A kind of continuous stratification tank | |
| CN202849055U (en) | Chlorine dioxide generation device | |
| CN205731169U (en) | A kind of reactor | |
| CN204395979U (en) | A kind of Raney's nickel making apparatus of improvement | |
| CN209423574U (en) | A kind of sodium hypochlorite synthetic tower | |
| CN204162411U (en) | Dry hydrogen production equipment | |
| CN204247173U (en) | The solid-liquid reaction gas generating unit that a kind of gas speed is adjustable | |
| CN211070028U (en) | Gas generating device and gaseous preparation experimental apparatus of high security | |
| CN206014411U (en) | Chlorine dioxide generator | |
| CN204601696U (en) | Liquid material extraction and isolation device | |
| CN208394784U (en) | A kind of chemical process CO 2 generator | |
| CN205472695U (en) | Bottom device of carbide stove | |
| CN201862367U (en) | Dissolving tank | |
| CN207698345U (en) | A kind of liquid container having sealing inner bag | |
| CN101058016B (en) | Fire-extinguishing system capable of continuously preparing carbon dioxide and its method for preparing carbon dioxide | |
| CN207158807U (en) | A kind of device for being used to balance titanium tetrachloride pressure inside the tank | |
| CN205235615U (en) | Bag type dust remover | |
| CN201342340Y (en) | Safety explosion proof type sodium hydride adder | |
| CN217042484U (en) | Acid adding device for chemical production acid adjusting kettle |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |