CN205462192U - Enamel reactor of recovery can be concentrated to tail gas - Google Patents
Enamel reactor of recovery can be concentrated to tail gas Download PDFInfo
- Publication number
- CN205462192U CN205462192U CN201620296589.9U CN201620296589U CN205462192U CN 205462192 U CN205462192 U CN 205462192U CN 201620296589 U CN201620296589 U CN 201620296589U CN 205462192 U CN205462192 U CN 205462192U
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- Prior art keywords
- tank body
- tail gas
- reaction still
- enamel reaction
- waste gas
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Abstract
The utility model discloses an enamel reactor of recovery can be concentrated to tail gas belongs to the chemical industry equipment field. It includes hollow jar of body, agitating unit and draught fan, the top of the jar body be equipped with feed inlet and exhaust outlet, the bottom is equipped with the discharge gate, agitating unit set up the top at the jar body, the draught fan be equipped with inlet scoop and air outlet, the inlet scoop of draught fan is passed through the pipeline and is connected with jar exhaust outlet of the body. The utility model discloses can retrieve the waste gas that produces in the reaction, avoid waste gas directly to emit into the air, the environmental pollution who causes, workshop operational environment worsens, and producers are healthy in harm, especially a plurality of reation kettle can adopt a suction fan to carry out tail gas and concentrate the collection, have simplified waste gas recovery laying pipeline, reduce equipment area, reduction in production cost, waste gas recovery convenient and fast.
Description
Technical field
This utility model belongs to field of chemical equipment, more particularly, it relates to a kind of tail gas can the enamel reaction still of centralized recovery.
Background technology
Enamel reaction still is by the glass containing high silicon dioxide, serves as a contrast the inner surface at steel vessel, the closeest through high temperature sintering
On metal surface, become composite product.So, it has stability and the two-fold advantage of metal strength of glass, is
A kind of excellent corrosion resistant apparatus.Glassed steel reaction vessels is widely used in the industry such as chemical industry, oil, medicine, pesticide, food.
Enamel reaction still, split and two kinds of structures of enclosed, open type is that body lid separates, and centre mat and clamp couple together, typically
It is that volume is at below 5000L；Enclosed is body-cover integrated, and general volume is at more than 5000L.Both structures respectively have superiority,
Open type dismounting is more convenient, if the mouth of pipe on cover goes wrong, is then easily detached individually repairing, enclosed then sealing property
It is better.In general, open architecture also has downhand welding dock Flange joint and flat lid type two kinds.
Enamel reaction still in the course of the work, along with the operation of agitating device, and the carrying out of reaction, can produce tail gas in tank body,
These tail gas contain composition that is harmful and that pollute environment, and the tail gas that reaction is produced by existing enamel reaction still is substantially
It is directly discharged in air, not only pollutes environment, also make Workshop Production ecological deterioration, producers' health is worked the mischief.This
Outward, in workshop, the most all there is multiple enamel reaction still, if each reactor individually carries out vent gas treatment, take up an area face
Long-pending big, efficiency is low, and production cost is high.
Through retrieval, China Patent Publication No. is: CN 202356095 U, and publication date is: the patent documentation on August 1st, 2012,
Disclose a kind of enamel reaction still, including: shell, enamel internal heater, agitator and condensate collector, in described enamel
Heater is arranged on enclosure, and described agitator is arranged on the inside center of enamel internal heater, in described enamel internal heater
Evenly distributed have add heat pipe, described shell is provided with steam inlet pipe and condensate outlet pipe, described steam inlet pipe connects and adds
Heat pipe, described condensate outlet pipe connects condensate collector.By the way, the enamel reaction still of this utility model is simple
Practicality, small investment, it is possible to ensureing that the reaction of reactor materials inside is fully complete, the utilization rate of steam is high, and heat loss is little, right
Material be mixed with catalytic intensification effect.
And for example, China Patent Publication No. is: CN 203281308 U, and publication date is: the patent documentation on November 13rd, 2013,
Disclosing a kind of enamel reaction still, it includes actuating device, axle envelope, shaft, bearing, chuck, kettle, agitator and subtracts
Shake plate, actuating device is connected with shaft, and shaft is located in kettle, and shaft and kettle junction are provided with axle envelope, still
External body is arranged on bearing by chuck, and shaft lower end is provided with agitator, and agitator is provided with shaft connecting place and subtracts
Shake plate.This utility model simple in construction, it is possible to reduce vibrations, thus ensure that reactor normally works, substantially increases production effect
Rate.
Above-mentioned two scheme is not the most the improvement that the vent gas treatment for enamel reaction still is carried out, and the tail gas produced after they reactions is straight
Run in air, pollute environment, be detrimental to health, be further improved.
Summary of the invention
1, problem to be solved
Not having tail gas treating function for existing enamel reaction still, the tail gas of generation is directly discharged in air, pollutes environment, danger
The problem of victimization body, this utility model provides a kind of tail gas can the enamel reaction still of centralized recovery, it is possible to produce in its work process
Raw tail gas carries out reclaiming pending, it is to avoid tail gas directly discharges the harm brought, when particularly multiple reactors being produced simultaneously,
Energy centralized recovery tail gas, reduces tail gas recycle difficulty, reduces occupation area of equipment, reduces production cost.
2, technical scheme
For solving the problems referred to above, this utility model adopts the following technical scheme that.
A kind of tail gas can the enamel reaction still of centralized recovery, including tank body, agitating device and the air-introduced machine of hollow；Described tank body
Top be provided with charging aperture and waste gas outlet, bottom is provided with discharging opening；Described agitating device is arranged on the top of tank body；Described
Air-introduced machine be provided with inlet scoop and air outlet, the inlet scoop of air-introduced machine is connected with the waste gas outlet of tank body by pipeline.
As further improvement of the utility model, described agitating device includes motor and shaft；Described motor is arranged on
The top of tank body；Described shaft stretches in tank body, and its lower end is provided with stirring vane；Described shaft is driven by motor
Dynamic.
As further improvement of the utility model, outside described tank body, it is coated with interlayer body；Described interlayer body and tank body
Airtight cavity is formed between outer surface.
As further improvement of the utility model, the top of described interlayer body is provided with steam inlet, and bottom is provided with condensed water and goes out
Mouthful.
As further improvement of the utility model, in described tank body, it is provided with thermometer boss, in thermometer boss, is provided with temperature
Meter.
As further improvement of the utility model, the top of described tank body is provided with manhole with sight glass.
As further improvement of the utility model, at the waste gas outlet of described tank body, it is provided with stop valve.
As further improvement of the utility model, the discharging opening of described tank body is provided with baiting valve.
As further improvement of the utility model, the inner surface of described tank body is attached with glass-lined coating；Described glass-lined coating
Thickness be 1.0-1.8mm.
3, beneficial effect
Compared to prior art, the beneficial effects of the utility model are:
(1) a kind of tail gas of the present utility model can the enamel reaction still of centralized recovery, tank body is offered waste gas outlet, and waste gas
Outlet is connected with the inlet scoop of induced-draught fan by pipeline, and the waste gas produced in reactor work process can be extracted out by induced-draught fan, so
After focus on being transported to exhaust-gas treatment, it is to avoid waste gas is directly discharged in air, and the environmental pollution caused, Yi Jizao
Becoming shopwork ecological deterioration, producers are healthy in harm；Particularly in the workshop containing multiple reactors, tank body
Waste gas outlet is connected to same induced-draught fan by pipeline, it is possible to concentrates and carries out tail gas recycle, can simplify waste gas recovery pipeline and lay,
Reducing occupation area of equipment, reduce production cost, waste gas recovery is convenient and swift；
(2) a kind of tail gas of the present utility model can the enamel reaction still of centralized recovery, the setting of agitating device, motor drives stirring
Axle rotates, and drives stirring vane work, is stirred reaction mass in tank body so that it is mix homogeneously, improves response speed,
Reaction is more abundant, and the top that the waste gas being also beneficial to reaction generation is discharged in tank body, facilitates induced-draught fan to extract out；
(3) a kind of tail gas of the present utility model can the enamel reaction still of centralized recovery, tank body outer cladding interlayer body, interlayer body and tank
Forming cavity between external surface, the steam inlet from interlayer body is passed through steam in this cavity, can heat tank body,
Make tank body reach to react temperature required, after steam cooling fluid chemical conversion water, discharge from condensation-water drain, the most repeatedly, reach to continue
The purpose of heating；
(4) a kind of tail gas of the present utility model can the enamel reaction still of centralized recovery, be provided with thermometer boss, thermometer in tank body
Thermometer it is provided with in sleeve pipe, in work process, thermometer display tank body temperature, monitor reaction temperature in real time；
(5) a kind of tail gas of the present utility model can the enamel reaction still of centralized recovery, tank body is provided with manhole with sight glass, staff
By it, reactor can be observed, debug, overhaul, safeguard, the operation such as cleaning；
(6) a kind of tail gas of the present utility model can the enamel reaction still of centralized recovery, be provided with stop valve at the waste gas outlet of tank body,
The opening and closing of waste gas outlet can be controlled according to job demand at any time, when the most multiple reactors are simultaneously connected with an induced-draught fan, protect
Demonstrate,prove waste gas recovery between each reactor separate, be independent of each other；
(7) a kind of tail gas of the present utility model can the enamel reaction still of centralized recovery, the discharging opening of tank body is provided with baiting valve, behaviour
Facilitate, open freely, motion flexibility and reliability, the convenient control to blowing；
(8) a kind of tail gas of the present utility model can the enamel reaction still of centralized recovery, the glass-lined coating thickness of tank inner surface attachment
Controlling between 1.0-1.8mm, reasonable in design, considering production needs to obtain with production cost；
(9) a kind of tail gas of the present utility model can the enamel reaction still of centralized recovery, simple in construction, reasonable in design, it is easy to manufacture.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1, tank body；2, charging aperture；3, discharging opening；4, motor；5, shaft；6, stirring vane；7, waste gas
Outlet；8, air-introduced machine；9, stop valve；10, interlayer body；11, steam inlet；12, condensation-water drain；13, thermometer
Sleeve pipe；14, manhole with sight glass.
Detailed description of the invention
Below in conjunction with specific embodiments and the drawings, this utility model is further described below.
Embodiment 1
As it is shown in figure 1, a kind of tail gas of the present embodiment can the enamel reaction still of centralized recovery, including tank body 1, the stirring of hollow
Device and air-introduced machine 8.Wherein, the top of described tank body 1 is provided with charging aperture 2 and waste gas outlet 7, and bottom is provided with discharging opening 3,
Discharging opening 3 is provided with baiting valve.In the present embodiment, thermometer boss 13, thermometer boss 13 it are provided with in described tank body 1
Inside it is provided with thermometer, temperature in tank body 1 can be monitored in real time；The top of tank body 1 is provided with manhole with sight glass 14, and staff is permissible
By it, reactor observed, debug, overhaul, safeguard, the operation such as cleaning；Interlayer body 10 it is coated with outside tank body 1,
Airtight cavity is formed between the outer surface of interlayer body 10 and tank body 1；The top of described interlayer body 10 is provided with steam inlet 11,
Bottom is provided with condensation-water drain 12, and steam inlet 11 all connects with airtight cavity with condensation-water drain 12；Described tank body 1
Inner surface be attached with glass-lined coating, the thickness of glass-lined coating is 1.0mm.
Described agitating device is arranged on the top of tank body 1.Specific in the present embodiment, described agitating device includes motor 4
With shaft 5；Described motor 4 is arranged on the top of tank body 1；Described shaft 5 stretches in tank body 1, and its lower end is pacified
Equipped with stirring vane 6；Described shaft 5 is driven by motor 4.
Described air-introduced machine 8 is provided with inlet scoop and air outlet, and the inlet scoop of air-introduced machine 8 is by the waste gas outlet of pipeline with tank body 1
7 connect, and the air outlet of air-introduced machine 8 leads to vent gas treatment ground by pipeline, and is provided with cut-off at the waste gas outlet 7 of tank body 1
Valve 9.In the present embodiment, tank body 1 has two, and their waste gas outlet 7 is connected to same air-introduced machine 8 by pipeline respectively
Inlet scoop, so, waste gas in two tank bodies 1 can be extracted with an air-introduced machine 8.
Time specifically used, adding the required material of reaction by charging aperture 2 in tank body 1, motor 4 drives shaft 5 to rotate,
Drive stirring vane 6 that material in tank body 1 is stirred；Meanwhile, it is passed through steam ground tank body 1 by steam inlet 11 to add
Heat, the condensed water formed after steam heat radiation liquefaction flows out from condensation-water drain 12, the most repeatedly, it is ensured that the continuous heating of tank body 1；
In thermometer boss 13, reaction temperature is monitored by thermometer in real time, it is ensured that reaction temperature is in reaction claimed range；React
Bi Hou, opens the baiting valve at discharging opening 3, discharges finished product, opening stop valve 9, and air-introduced machine 8 works, by useless in tank body 1
Gas is extracted out, is transported to corresponding vent gas treatment ground, focuses on.
A kind of tail gas of the present utility model can the enamel reaction still of centralized recovery, the waste gas produced in reaction can be reclaimed, keep away
Exempt from waste gas and be directly discharged into air, the environmental pollution caused, and make shopwork ecological deterioration, producers are healthy in harm；
The most multiple reactors use an induced-draught fan to carry out tail gas centralized collection, simplify waste gas recovery pipeline and lay, reduce equipment
Floor space, reduces production cost, and waste gas recovery is convenient and swift.
Embodiment 2
A kind of tail gas of the present embodiment can the enamel reaction still of centralized recovery, substantially the same manner as Example 1, difference is:
The inner surface of described tank body 1 is attached with glass-lined coating, and the thickness of glass-lined coating is 1.5mm.
Embodiment 3
A kind of tail gas of the present embodiment can the enamel reaction still of centralized recovery, substantially the same manner as Example 1, difference is:
The inner surface of described tank body 1 is attached with glass-lined coating, and the thickness of glass-lined coating is 1.8mm.
Schematically being described this utility model and embodiment thereof above, this description does not has restricted, shown in accompanying drawing
Be also one of embodiment of the present utility model, actual structure is not limited thereto.So, if this area is common
Technical staff is enlightened by it, in the case of creating objective without departing from this utility model, designs and this technology without creative
Frame mode that scheme is similar and embodiment, all should belong to protection domain of the present utility model.
Claims (9)
1. tail gas can the enamel reaction still of centralized recovery, including the tank body (1) of hollow, it is characterised in that: also include stirring
Mix device and air-introduced machine (8)；The top of described tank body (1) is provided with charging aperture (2) and waste gas outlet (7), and bottom sets
There is discharging opening (3)；Described agitating device is arranged on the top of tank body (1)；Described air-introduced machine (8) be provided with inlet scoop and
Air outlet, the inlet scoop of air-introduced machine (8) is connected with the waste gas outlet (7) of tank body (1) by pipeline.
A kind of tail gas the most according to claim 1 can the enamel reaction still of centralized recovery, it is characterised in that: described stirring
Device includes motor (4) and shaft (5)；Described motor (4) is arranged on the top of tank body (1)；Described stirring
Axle (5) stretches in tank body (1), and its lower end is provided with stirring vane (6)；Described shaft (5) passes through motor (4)
Drive.
A kind of tail gas the most according to claim 1 can the enamel reaction still of centralized recovery, it is characterised in that: described tank body
(1) outside is coated with interlayer body (10)；Formed airtight between described interlayer body (10) and the outer surface of tank body (1)
Cavity.
A kind of tail gas the most according to claim 3 can the enamel reaction still of centralized recovery, it is characterised in that: described interlayer
The top of body (10) is provided with steam inlet (11), and bottom is provided with condensation-water drain (12).
5. can the enamel reaction still of centralized recovery according to a kind of tail gas described in any one in claim 3, it is characterised in that:
Being provided with thermometer boss (13) in described tank body (1), thermometer boss is provided with thermometer in (13).
6. can the enamel reaction still of centralized recovery according to a kind of tail gas described in any one in claim 1-5, it is characterised in that:
The top of described tank body (1) is provided with manhole with sight glass (14).
A kind of tail gas the most according to claim 1 can the enamel reaction still of centralized recovery, it is characterised in that: described tank body
(1) waste gas outlet (7) place is provided with stop valve (9).
A kind of tail gas the most according to claim 1 can the enamel reaction still of centralized recovery, it is characterised in that: described tank body
(1) discharging opening (3) is provided with baiting valve.
9. can the enamel reaction still of centralized recovery according to a kind of tail gas described in claim 7 or 8, it is characterised in that: described
The inner surface of tank body (1) is attached with glass-lined coating；The thickness of described glass-lined coating is 1.0-1.8mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620296589.9U CN205462192U (en) | 2016-04-08 | 2016-04-08 | Enamel reactor of recovery can be concentrated to tail gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620296589.9U CN205462192U (en) | 2016-04-08 | 2016-04-08 | Enamel reactor of recovery can be concentrated to tail gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205462192U true CN205462192U (en) | 2016-08-17 |
Family
ID=56645020
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620296589.9U Expired - Fee Related CN205462192U (en) | 2016-04-08 | 2016-04-08 | Enamel reactor of recovery can be concentrated to tail gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205462192U (en) |
-
2016
- 2016-04-08 CN CN201620296589.9U patent/CN205462192U/en not_active Expired - Fee Related
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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: 20160817 Termination date: 20180408 |