CN206160556U - Reation kettle heat recovery heat pump system with clean function of waste water - Google Patents
Reation kettle heat recovery heat pump system with clean function of waste water Download PDFInfo
- Publication number
- CN206160556U CN206160556U CN201621194129.1U CN201621194129U CN206160556U CN 206160556 U CN206160556 U CN 206160556U CN 201621194129 U CN201621194129 U CN 201621194129U CN 206160556 U CN206160556 U CN 206160556U
- Authority
- CN
- China
- Prior art keywords
- reactor
- waste water
- evaporation tank
- reation kettle
- cooling cylinder
- 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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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Abstract
The utility model discloses a reation kettle heat recovery heat pump system with clean function of waste water, the control unit comprises a reaction vessel, reation kettle's outer wall fixedly connected with seals the intermediate layer, and it has sewage pipes to seal the switch -on of interbedded left side wall body upper portion, the beneficial effects of the utility model are that: the exothermic liquid that becomes of freon condensation liquefaction behind the condenser of entering evaporation incasement, to evaporate the waste water heating of incasement, high temperature water vapor passes through the chemical industry carbon plate, air exhauster and steam conduit enter into in the reation kettle, provide required vapor and temperature for reation kettle, the intermediate layer is sealed in the waste water circulation, provide required heat to reation kettle, in more vapor enters into the cooling cylinder through the steam backflow pipeline in the reation kettle, when getting into the evaporimeter in the cooling cylinder, freon gasification heat absorption becomes gas, begin next circulation through the compressor once more, vapor is become clean liquid water by the condensation in entering into the cooling cylinder.
Description
Technical field
The utility model is related to a kind of waste heat recovery device, specifically a kind of reactor with waste water cleaning function
Recuperation of heat utilizes heat pump.
Background technology
Most reactor needs suitable temperature and humidity that the raw material in reactor can just fully reacted, and one
As reactor be required for supporting steam generator and temperature-adjusting heating device, although supporting steam generator and temperature heating
Device ensure that the raw material in reactor is reacted, but supporting device is all a kind of for enterprise or factory
Burden, if high-volume is using this reactor and corollary apparatus, needs to spend more cost.
Reactor waste-heat recovery device is disclosed in Granted publication is for the Chinese patent of CN205392380U, the device energy
Enough by the energy absorption of the high-temperature vapor in interlayer, but the device needs steam generator to generate high-temperature vapor, and
And the energy that absorbs of the device can not be acted on preferably reactor again.
Utility model content
The purpose of this utility model is to provide a kind of reactor recuperation of heat with waste water cleaning function to utilize heat pump system
System, to solve the problems, such as above-mentioned background technology in propose.
For achieving the above object, the utility model provides following technical scheme：
A kind of reactor recuperation of heat with waste water cleaning function utilizes heat pump, including reactor, the reactor
Outer wall be fixedly connected with closed sandwich, the left side wall body top of closed sandwich is connected blow-off line, a left side for the reactor
Side is installed with evaporation tank, and the inside of evaporation tank is provided with condenser, cooling cylinder is provided with the right side of evaporation tank, solid in cooling cylinder
Dingan County is equipped with evaporimeter, and upper end of evaporator mouth is connected with the upper port of condenser by upper pipeline, installs on the upper pipeline
There is expansion valve, the lower port of evaporimeter is connected with the lower port of condenser by lower pipeline, pressure is installed on the lower pipeline
Built with freon, the left side wall body of the evaporation tank offers dirt-discherging outlet for contracting machine, the upper pipeline and lower pipeline, evaporation tank with
Closed sandwich is connected by dirt-discherging outlet, and the upper inside of evaporation tank is fixedly connected with chemical industry carbon slab, the top of the evaporation tank
Air exhauster is installed with, the air inlet of air exhauster is located at the inside of evaporation tank, and the upper end of air exhauster is connected jet chimney, steams
Steam pipe road is connected with the top of reactor, and the top of the reactor passes through Steam Recovery pipeline phase with the upper wall body of cooling cylinder
Connect.
As further program of the utility model：Rear pump and flow control valve are installed on the blow-off line.
As the utility model further scheme：The upside wall body right side of the evaporation tank is connected sewage conduct.
As the utility model further scheme：The right side wall body bottom of the cooling cylinder is connected drainage pipeline.
As the utility model further scheme：The condenser is one or one group of immersed condensator.
As the utility model further scheme：The evaporimeter is one or one group of immersion type evaporimeter.
Compared with prior art, the beneficial effects of the utility model are：Freon is cold into after the condenser in evaporation tank
Solidifying liquidation exothermic reaction becomes liquid, and the waste water in evaporation tank is heated, and high-temperature vapor passes through chemical industry carbon plate, air exhauster and steam pipe
Road is entered into reactor, the vapor and temperature required for providing for reactor, waste water circulation closed sandwich, and reactor is carried
For required heat, more vapor is entered into cooling cylinder by vapor return line in reactor, into cooling cylinder
During interior evaporimeter, freon gasification heat absorption becomes gas, circulates again by compressor starts are next, and vapor is entered into
Clean liquid water is condensed into cooling cylinder.
Description of the drawings
Fig. 1 is a kind of structural representation of reactor recuperation of heat with waste water cleaning function using heat pump.
In figure：1- reactors, 2- closed sandwich, 3- blow-off lines, 4- evaporation tanks, 5- condensers, 6- cooling cylinders, 7- evaporations
Pipeline, 11- compressors, 12- freon, 13- dirt-discherging outlets, 14- chemical industry carbon slabs, 15- under the upper pipeline of device, 8-, 9- expansion valves, 10-
Air exhauster, 16- jet chimneys, 17- vapor return lines, 18- sewage conducts, 19- drainage pipelines, 20- rear pumps, 21- flows
Regulating valve.
Specific embodiment
The technical scheme of this patent is described in more detail with reference to specific embodiment.
Fig. 1 is referred to, a kind of reactor recuperation of heat with waste water cleaning function utilizes heat pump, including reactor 1,
The outer wall of the reactor 1 is fixedly connected with closed sandwich 2, and the left side wall body top of closed sandwich 2 is connected blow-off line 3,
The left side of the reactor 1 is installed with evaporation tank 4, and the inside of evaporation tank 4 is provided with condenser 5, and the right side of evaporation tank 4 sets
Have in cooling cylinder 6, cooling cylinder 6 and be installed with evaporimeter 7, the upper port of evaporimeter 7 passes through upper pipe with the upper port of condenser 5
Road 8 is connected, and expansion valve 9 is provided with the upper pipeline 8, and the lower port of evaporimeter 7 is with the lower port of condenser 5 by lower pipeline
10 are connected, and compressor 11 is provided with the lower pipeline 10, and the upper pipeline 8 and lower pipeline 10 are built with Freon 12, institute
The left side wall body for stating evaporation tank 4 offers dirt-discherging outlet 13, and evaporation tank 4 is connected with closed sandwich 2 by dirt-discherging outlet 13, evaporation tank
4 upper inside is fixedly connected with chemical industry carbon slab 14, and the top of the evaporation tank 4 is installed with air exhauster 15, air exhauster 15
Air inlet be located at the inside of evaporation tank 4, the upper end of air exhauster 15 is connected jet chimney 16, jet chimney 16 and reactor 1
Top be connected, the top of the reactor 1 is connected with the upper wall body of cooling cylinder 6 by Steam Recovery pipeline 17；
Waste water is injected into evaporation tank 4, and the Freon 12 in lower side conduit is by compressor 11 plus presses to HTHP gas
Body, the 5 Freon 12 condensation liquefaction heat releases into after the condenser in evaporation tank 4 become liquid, and the waste water in evaporation tank 4 is added
Heat, high-temperature vapor is entered into reactor 1 by chemical industry carbon plate 14, air exhauster 15 and jet chimney 16, is that reactor 1 is provided
Required vapor and temperature, the waste water containing impurity is discharged by dirt-discherging outlet 13, closed sandwich 2 and blow-off line 3, is given up
Current lead to closed sandwich 2, provide reactor 1 required heat, and more vapor passes through opposing steam flow pipe in reactor 1
Road 17 is entered into cooling cylinder 6, and the Freon 12 for becoming liquid is reduced pressure through expansion valve 9, the evaporation into cooling cylinder 6
During device 7, Freon 12 gasification heat absorption becomes gas, starts next circulation again by compressor 11, now in cooling cylinder 6
Temperature is reduced, and vapor is entered into cooling cylinder 6 and is condensed into liquid water, and now liquid water is clean liquid water.
Rear pump 20 and flow control valve 21 are installed on the blow-off line 3.
The upside wall body right side of the evaporation tank 4 is connected sewage conduct 18.
The right side wall body bottom of the cooling cylinder 6 is connected drainage pipeline 19.
The condenser 5 is one or one group of immersed condensator.
The evaporimeter 7 is one or one group of immersion type evaporimeter.
Operation principle of the present utility model is：Waste water is injected into evaporation tank 4, and the Freon 12 in lower side conduit is compressed
Machine 11 plus high temperature and high pressure gas are pressed to, the 5 Freon 12 condensation liquefaction heat releases into after the condenser in evaporation tank 4 become liquid
Body, the waste water in evaporation tank 4 is heated, and high-temperature vapor is entered into by chemical industry carbon plate 14, air exhauster 15 and jet chimney 16
It is the vapor and temperature required for reactor 1 is provided in reactor 1, the waste water containing impurity is by dirt-discherging outlet 13, closing folder
Layer 2 and blow-off line 3 are discharged, waste water circulation closed sandwich 2, reactor 1 is provided in required heat, reactor 1 compared with
Many vapor is entered into cooling cylinder 6 by vapor return line 17, is become the Freon 12 of liquid and is carried out through expansion valve 9
Decompression, during into evaporimeter 7 in cooling cylinder 6, Freon 12 gasification heat absorption becomes gas, under starting again by compressor 11
One circulation, the now temperature reduction in cooling cylinder 6, vapor is entered into cooling cylinder 6 and is condensed into liquid water, now liquid
Water is clean liquid water.
It is obvious to a person skilled in the art that the utility model is not limited to the details of above-mentioned one exemplary embodiment, and
And in the case of without departing substantially from spirit or essential attributes of the present utility model, can in other specific forms realize that this practicality is new
Type.Therefore, no matter from the point of view of which point, embodiment all should be regarded as exemplary, and is nonrestrictive, this practicality is new
The scope of type is by claims rather than described above is limited, it is intended that the equivalency fallen in claim is contained
All changes in justice and scope are included in the utility model.Any reference in claim should not be considered as restriction
Involved claim.
Moreover, it will be appreciated that although this specification is been described by according to embodiment, not each embodiment is only wrapped
Containing an independent technical scheme, this narrating mode of specification is only that for clarity those skilled in the art should
Using specification as an entirety, the technical scheme in each embodiment can also Jing it is appropriately combined, form those skilled in the art
Understandable other embodiment.
Claims (6)
1. a kind of reactor recuperation of heat with waste water cleaning function utilizes heat pump, including reactor, it is characterised in that institute
The outer wall for stating reactor is fixedly connected with closed sandwich, and the left side wall body top of closed sandwich is connected blow-off line, described anti-
Answer and be installed with the left of kettle evaporation tank, the inside of evaporation tank is provided with condenser, and cooling cylinder is provided with the right side of evaporation tank, cold
Evaporimeter is installed with solidifying case, upper end of evaporator mouth is connected with the upper port of condenser by upper pipeline, the upper pipe
Expansion valve is installed, the lower port of evaporimeter is connected with the lower port of condenser by lower pipeline on road, on the lower pipeline
Compressor is installed, built with freon, the left side wall body of the evaporation tank offers dirt-discherging outlet for the upper pipeline and lower pipeline,
Evaporation tank is connected with closed sandwich by dirt-discherging outlet, and the upper inside of evaporation tank is fixedly connected with chemical industry carbon slab, the evaporation
The top of case is installed with air exhauster, and the air inlet of air exhauster is located at the inside of evaporation tank, and the upper end of air exhauster is connected steaming
Steam pipe road, jet chimney is connected with the top of reactor, and the top of the reactor passes through steam with the upper wall body of cooling cylinder
Recovery channel is connected.
2. a kind of reactor recuperation of heat with waste water cleaning function according to claim 1 utilizes heat pump, and it is special
Levy and be, rear pump and flow control valve are installed on the blow-off line.
3. a kind of reactor recuperation of heat with waste water cleaning function according to claim 1 and 2 utilizes heat pump, its
It is characterised by, the upside wall body right side of the evaporation tank is connected sewage conduct.
4. a kind of reactor recuperation of heat with waste water cleaning function according to claim 3 utilizes heat pump, and it is special
Levy and be, the right side wall body bottom of the cooling cylinder is connected drainage pipeline.
5. a kind of reactor recuperation of heat with waste water cleaning function according to claim 1 utilizes heat pump, and it is special
Levy and be, the condenser is one or one group of immersed condensator.
6. a kind of reactor recuperation of heat with waste water cleaning function according to claim 5 utilizes heat pump, and it is special
Levy and be, the evaporimeter is one or one group of immersion type evaporimeter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621194129.1U CN206160556U (en) | 2016-10-28 | 2016-10-28 | Reation kettle heat recovery heat pump system with clean function of waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621194129.1U CN206160556U (en) | 2016-10-28 | 2016-10-28 | Reation kettle heat recovery heat pump system with clean function of waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206160556U true CN206160556U (en) | 2017-05-10 |
Family
ID=58657722
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621194129.1U Expired - Fee Related CN206160556U (en) | 2016-10-28 | 2016-10-28 | Reation kettle heat recovery heat pump system with clean function of waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206160556U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108636086A (en) * | 2018-07-11 | 2018-10-12 | 安徽京仪自动化装备技术有限公司 | A kind of heating plant of purification manufacture of semiconductor exhaust gas |
-
2016
- 2016-10-28 CN CN201621194129.1U patent/CN206160556U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108636086A (en) * | 2018-07-11 | 2018-10-12 | 安徽京仪自动化装备技术有限公司 | A kind of heating plant of purification manufacture of semiconductor exhaust gas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20170510 Termination date: 20171028 |