CN205653429U - Device of bio diesel oil by -product glycerine - Google Patents
Device of bio diesel oil by -product glycerine Download PDFInfo
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- CN205653429U CN205653429U CN201620301498.XU CN201620301498U CN205653429U CN 205653429 U CN205653429 U CN 205653429U CN 201620301498 U CN201620301498 U CN 201620301498U CN 205653429 U CN205653429 U CN 205653429U
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- heat exchanger
- distillation column
- byproduct
- biology
- steam pipe
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Abstract
The utility model relates to a glycerine production facility technical field, concretely relates to device of bio diesel oil by -product glycerine, including distillation column, transfer line, heat exchanger and steam pipe, the entry end of transfer line and the lower part of distillation column intercommunication, the exit end of transfer line and the bottom of heat exchanger intercommunication, the entry end of steam pipe and the top of heat exchanger intercommunication, the exit end of steam pipe and the top of distillation column intercommunication, the transfer line is provided with the power cycle pump. Under the positive action of power cycle pump, salinity speed of scale deposit in the heat exchanger is slower, even more seriously influence when production in the salinity scale deposit, lets in the heat exchanger with this pump with hot water, and very conveniently the salinity with the scale deposit dissolves the discharge, and is very little to the influence of production, fast convenient, material flow rate is accelerated to powerful circulating pump, and heat time is short, is applicable to high viscosity, heat sensitive material such as biodiesel.
Description
Technical field
This utility model relates to glycerol production equipment technical field, is specifically related to a kind of device producing glycerol being as byproduct of biology.
Background technology
The ratio non-renewable resources such as oil, reproducible biodiesel more development potentiality.Along with the production scale of biodiesel goes from strength to strength, its side-product, the yield of the side-product crude glycerine of biodiesel the most constantly increases.Prior art typically uses traditional liter membrane type glycerol distillation device to refine glycerol, raw material is driven to rise to distillation column under vapor action, but contain the salinity of about 5 ~ 10% inside biodiesel crude glycerine, the easy fouling of heat exchanger in process of production, hindering the transport of raw material, if clear up not in time simultaneously, then salinity fouling can be difficult to clean off, and traditional firing rate rising membrane type glycerol distillation device is slowly, production efficiency is low.
Summary of the invention
The purpose of this utility model is for above-mentioned deficiency of the prior art, it is provided that a kind of forced circulation, the device producing glycerol being as byproduct of biology that heat time heating time is short, material flow is fast.
The purpose of this utility model is achieved through the following technical solutions:
A kind of device producing glycerol being as byproduct of biology, including distillation column, tube for transfusion, heat exchanger and steam pipe, the arrival end of described tube for transfusion connects with the bottom of distillation column, the port of export of described tube for transfusion connects with the bottom of heat exchanger, the arrival end of described steam pipe connects with the top of heat exchanger, the port of export of described steam pipe connects with the top of distillation column, and described tube for transfusion is provided with power cycle pump.
Wherein, described distillation column bottom is provided with manhole, and described manhole is provided with form.
Wherein, described heat exchanger is tubular heat exchanger.
Wherein, described distillation column is provided with water inlet.
Wherein, described distillation column top is provided with steam (vapor) outlet, and described steam (vapor) outlet is provided with switch valve.
Wherein, described power cycle pump is centrifugal pump.
Wherein, it is provided with hydrostatic gauge bottom described distillation column.
Wherein, described heat exchanger is made up of heat-exchanging chamber and heat exchanger tube, and described heat exchanger tube and a ultrasonic activation generating mechanism connect.
The beneficial effects of the utility model: 1, under the positive action of power cycle pump, salinity speed of fouling in heat exchanger is slower, even if when salinity fouling is compared and is had a strong impact on production, with this pump, hot water is passed through in heat exchanger, easily the salinity of fouling is dissolved away discharge, impact on producing is the least, fast and easy；2, material flow accelerated by power cycle pump, and heat time heating time is short, it is adaptable to the high viscositys such as biodiesel, heat sensitive material.
Accompanying drawing explanation
Utilize accompanying drawing that utility model is described further, but the embodiment in accompanying drawing does not constitute any restriction of the present utility model, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to the following drawings.
Fig. 1 is structural representation of the present utility model.
Reference includes: 1-distillation column, 11-manhole, 12-water inlet, 13-steam (vapor) outlet, 14-hydrostatic gauge, 2-tube for transfusion, 3-heat exchanger, 31-heat-exchanging chamber, 32-heat exchanger tube, 33-ultrasonic activation generating mechanism, 4-steam pipe, 5-power cycle pump.
Detailed description of the invention
With the following Examples this utility model is further described.
A kind of device producing glycerol being as byproduct of biology, including distillation column 1, tube for transfusion 2, heat exchanger 3 and steam pipe 4, the arrival end of described tube for transfusion 2 connects with the bottom of distillation column 1, the port of export of described tube for transfusion 2 connects with the bottom of heat exchanger 3, the arrival end of described steam pipe 4 connects with the top of heat exchanger 3, the port of export of described steam pipe 4 connects with the top of distillation column 1, and described tube for transfusion 2 is provided with power cycle pump 5.
Under the positive action of power cycle pump 5, salinity speed of fouling in heat exchanger is relatively slow, even if when salinity fouling is compared and had a strong impact on production, with this pump, hot water is passed through in heat exchanger, easily the salinity of fouling being dissolved away discharge, the impact on producing is the least, fast and easy；And material flow accelerated by power cycle pump 5, heat time heating time is short, it is adaptable to the high viscositys such as biodiesel, heat sensitive material.
Wherein, described distillation column 1 bottom is provided with manhole 11, and described manhole 11 is provided with form.Manhole 11 set up in order to equipment break down time, facilitate maintainer to enter and repair, and the setting up of form, can directly observe the mobility status of material from the external world, it is judged that the fouling condition of heat exchanger 3.
Wherein, described heat exchanger 3 is tubular heat exchanger.Tubular heat exchanger 3 simple in construction, compact, cost convenience, coordinate the power cycle pump 5 of the present embodiment, it is possible to use hot water is carried out heat exchanger 3, improve tubular heat exchanger and clean the problem being difficult to.
Wherein, described distillation column 1 is provided with water inlet 12, and described water inlet 12 is provided with control valve.Warm wash water enters from water inlet 12, and power cycle pump 5 accelerates, and washes away the dirt of heat exchanger 3, simple and practical.
Wherein, described distillation column 1 top is provided with steam (vapor) outlet 13, and described steam (vapor) outlet 13 is provided with switch valve.Steam (vapor) outlet 13 can collect steam as two effect thermals source, economic and environment-friendly.
Wherein, described power cycle pump 5 is centrifugal pump.Centrifugal pump structure is compact, High power output, strengthens the scouring capability of warm wash water.
Wherein, it is provided with hydrostatic gauge 14 bottom described distillation column 1.Hydrostatic gauge 14 can help staff to judge whether equipment leaks, it is to avoid unnecessary loss.
Wherein, described heat exchanger 3 is made up of heat-exchanging chamber 31 and heat exchanger tube 32, and described heat exchanger tube 32 is connected with a ultrasonic activation generating mechanism 33.Ultrasonic activation generating mechanism 33 can upset the kinestate of heat exchanger tube 32 liquid, produces wadding stream, dirt can be made to come off from heat exchanger tube 32, reduce its scale velocity while improving heat exchanger effectiveness.
Finally should be noted that; above example is only in order to illustrate the technical solution of the utility model; rather than the restriction to this utility model protection domain; although having made to explain to this utility model with reference to preferred embodiment; it will be understood by those within the art that; the technical solution of the utility model can be modified or equivalent, without deviating from the spirit and scope of technical solutions of the utility model.
Claims (8)
1. the device producing glycerol being as byproduct of biology, it is characterized in that: include distillation column, tube for transfusion, heat exchanger and steam pipe, the arrival end of described tube for transfusion connects with the bottom of distillation column, the port of export of described tube for transfusion connects with the bottom of heat exchanger, the arrival end of described steam pipe connects with the top of heat exchanger, the port of export of described steam pipe connects with the top of distillation column, and described tube for transfusion is provided with power cycle pump.
A kind of device producing glycerol being as byproduct of biology the most according to claim 1, it is characterised in that: described distillation column bottom is provided with manhole, and described manhole is provided with form.
A kind of device producing glycerol being as byproduct of biology the most according to claim 1, it is characterised in that: described heat exchanger is tubular heat exchanger.
A kind of device producing glycerol being as byproduct of biology the most according to claim 1, it is characterised in that: described distillation column is provided with water inlet.
A kind of device producing glycerol being as byproduct of biology the most according to claim 1, it is characterised in that: described distillation column top is provided with steam (vapor) outlet, and described steam (vapor) outlet is provided with switch valve.
A kind of device producing glycerol being as byproduct of biology the most according to claim 1, it is characterised in that: described power cycle pump is centrifugal pump.
A kind of device producing glycerol being as byproduct of biology the most according to claim 1, it is characterised in that: it is provided with hydrostatic gauge bottom described distillation column.
A kind of device producing glycerol being as byproduct of biology the most according to claim 1, it is characterised in that: described heat exchanger is made up of heat-exchanging chamber and the heat exchanger tube being arranged in heat-exchanging chamber, and described heat exchanger tube and a ultrasonic activation generating mechanism connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620301498.XU CN205653429U (en) | 2016-04-12 | 2016-04-12 | Device of bio diesel oil by -product glycerine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620301498.XU CN205653429U (en) | 2016-04-12 | 2016-04-12 | Device of bio diesel oil by -product glycerine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205653429U true CN205653429U (en) | 2016-10-19 |
Family
ID=57389892
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620301498.XU Active CN205653429U (en) | 2016-04-12 | 2016-04-12 | Device of bio diesel oil by -product glycerine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205653429U (en) |
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2016
- 2016-04-12 CN CN201620301498.XU patent/CN205653429U/en active Active
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |