CN209188178U - A kind of heat-energy recovering apparatus - Google Patents

A kind of heat-energy recovering apparatus Download PDF

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Publication number
CN209188178U
CN209188178U CN201821685583.6U CN201821685583U CN209188178U CN 209188178 U CN209188178 U CN 209188178U CN 201821685583 U CN201821685583 U CN 201821685583U CN 209188178 U CN209188178 U CN 209188178U
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Prior art keywords
heat
heat exchanger
inlet
recovering apparatus
energy recovering
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CN201821685583.6U
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Chinese (zh)
Inventor
卢国定
陈国平
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NINGBO GREEN-HEALTH PHARMA-CEUTICAL Co Ltd
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NINGBO GREEN-HEALTH PHARMA-CEUTICAL Co Ltd
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Abstract

The utility model provides a kind of heat-energy recovering apparatus, belongs to pharmaceutical equipment technical field comprising: extract equipment is equipped with inlet and discharge port;Recycling machine, top are equipped with feed inlet and discharge the gas outlet of hot gas, and feed inlet is connected by conveyance conduit with discharge port;First Heat Exchanger, one end are connected with gas outlet, and the other end is connected with inlet;Solvent tank conveys cold cut matchmaker to the first heat exchanger, and the hot gas that cold cut matchmaker and gas outlet discharge forms thermosol matchmaker after heat exchange occurs, and thermosol matchmaker passes through inlet again and inputs extract equipment.The utility model has the advantages that energy saving.

Description

A kind of heat-energy recovering apparatus
Technical field
The utility model belongs to pharmaceutical equipment technical field, is related to a kind of heat-energy recovering apparatus.
Background technique
Solvent be it is a kind of can dissolved gas, solid, liquid and become homogeneous mixture liquid.It is some in pharmaceutical operations Material needs the dregs of a decoction temperature for being added in extract equipment together with solvent, and being heated to certain temperature to produce spice, after reaction Degree is still higher, and releasable certain heat is not handled the thermal energy of the dregs of a decoction generally, therefore there are heats in the prior art Waste, there are improved spaces.
Therefore, it is necessary to design a kind of energy saving heat-energy recovering apparatus.
Summary of the invention
The purpose of this utility model is the presence of the above problem in view of the prior art, proposes a kind of energy saving thermal energy Recyclable device
The purpose of this utility model can be realized by the following technical scheme: a kind of heat-energy recovering apparatus, comprising:
Extract equipment is equipped with inlet and discharge port;
Recycling machine, top are equipped with feed inlet and discharge the gas outlet of hot gas, and feed inlet passes through conveyance conduit and discharge port It is connected;
First Heat Exchanger, one end are connected with gas outlet, and the other end is connected with inlet;
Solvent tank conveys cold cut matchmaker to the first heat exchanger, after heat exchange occurs for the hot gas that cold cut matchmaker and gas outlet discharge Thermosol matchmaker is formed, thermosol matchmaker passes through inlet again and inputs extract equipment.
First heat exchanger is also connected with the second heat exchanger, solvent in turn as a further improvement of the utility model, Receiving tank, and coolant liquid, by the second heat exchanger, the hot gas of gas outlet release is after the output of the first heat exchanger, then is delivered to second Simultaneously with coolant liquid heat exchange occurs for heat exchanger, solvent is precipitated after hot gas condensation, solvent is stored by solvent pans.
Automatic temperature-adjusting tune is provided between first heat exchanger and inlet as a further improvement of the utility model, Save valve.
The recycling machine includes casing, rotatable rotary column as a further improvement of the utility model, casing from up to Under be separated to form at least two reclaiming chambers, material path connection is led between two reclaiming chambers of arbitrary neighborhood, the reclaiming chamber at top is set There are a gas outlet and feed inlet, rotary column is set to the center of casing and passes through all reclaiming chambers, is additionally provided in each reclaiming chamber and rotary column The pivoted arm being connected, the super discharge hole of arm length.
As a further improvement of the utility model, positioned at the material hole of reclaiming chamber at top, feed inlet centered on rotary column It is arranged symmetrically.
The quantity of the reclaiming chamber is five as a further improvement of the utility model, is connected to four material of reclaiming chamber Hole is successively rotated by 90 ° arrangement under upper centered on rotary column.
Each reclaiming chamber is correspondingly arranged on hatch door as a further improvement of the utility model,.
The solvent tank is located above extract equipment as a further improvement of the utility model, and inlet, which is set to, to be extracted At the top of equipment, discharge port is set to the bottom of extract equipment.
The tapered setting of the discharge port as a further improvement of the utility model,.
The feed inlet of the recycling machine is higher than the discharging of the extract equipment as a further improvement of the utility model, Mouthful, and conveying hoister is equipped in conveyance conduit.
Based on the above-mentioned technical proposal, the utility model embodiment at least can produce following technical effect:
1, material generates the dregs of a decoction with solvent after extract equipment is reacted, and the dregs of a decoction are discharged from discharge port and enter along conveyance conduit Recycling machine, the dregs of a decoction discharge thermal energy with the air in heating recovery machine, and according to the principle that hot-air rises, air after heating is from returning At gas outlet at the top of receipts machine discharge, hot-air and solvent tank output cold cut matchmaker occur in the first heat exchanger heat exchange type at Thermosol matchmaker, thermosol matchmaker inputs extract equipment by inlet again, thus realize the recycling of dregs of a decoction thermal energy, with energy saving, and It is directly higher to the production efficiency of extract equipment addition thermosol matchmaker compared to the scheme for improving reaction temperature in extract equipment.
2, the dregs of a decoction enter the accommodating chamber of recycling machine by feed inlet, and pivoted arm circumferentially rotates under rotary column drive, and the dregs of a decoction are through turning It falls after arm is broken up and from the separation of material hole, to accelerate the release of thermal energy, to make full use of the thermal energy in the dregs of a decoction, avoids dregs of a decoction heap Product can not discharge heat together, its long-time is caused to exchange with the concurrent heat of chassis contact, reduce the formation effect of hot-air Rate.
3, the material hole of the reclaiming chamber at top and feed inlet are symmetrically set in the two sides of rotary column, guarantee that the dregs of a decoction fall it from material hole Before, the dregs of a decoction possess sufficiently long rotation distance, and pivoted arm can sufficiently break up the dregs of a decoction, and heat releasing effect is more preferably.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of one preferred embodiment of the utility model.
Fig. 2 is the schematic diagram of internal structure of recycling machine.
Fig. 3 is the cross-sectional view of A-A in Fig. 2.
In figure, 100, extract equipment;110;Inlet;120, discharge port;200, conveyance conduit;300, recycling machine;310, Casing;320, reclaiming chamber;321, gas outlet;322, feed inlet;323, expect hole;330, rotary column;331, pivoted arm;340, hatch door; 400, the first heat exchanger;500, solvent tank;600, the second heat exchanger;700, solvent receiving tank;800, automatic temperature adjusting valve.
Specific embodiment
It is specific embodiment of the utility model and in conjunction with attached drawing below, the technical solution of the utility model is made further Description, but the utility model is not limited to these examples.
As shown in Figure 1 to Figure 3, this heat-energy recovering apparatus, comprising:
Extract equipment 100 is equipped with inlet 110 and discharge port 120;
Recycling machine 300, top are equipped with feed inlet 322 and discharge the gas outlet 321 of hot gas, and feed inlet 322 passes through conveying Pipeline 200 is connected with discharge port 120;
First Heat Exchanger 400, one end are connected with gas outlet 321, and the other end is connected with inlet 110;
Solvent tank 500 conveys cold cut matchmaker to the first heat exchanger 400, and the hot gas that cold cut matchmaker and gas outlet 321 discharge occurs Thermosol matchmaker is formed after heat exchange, thermosol matchmaker passes through inlet 110 again and inputs extract equipment 100.
In actual application, the thermosol matchmaker temperature requirement flowed out from solvent tank 500 is at 60 DEG C or so, and recycling machine The hot air temperature of 300 outflows is required at 70 DEG C or so, and extract equipment 100 is with heating device to guarantee reaction temperature.
Thermal energy removal process is as follows: material and solvent generate the dregs of a decoction after extract equipment 100 is reacted, and the dregs of a decoction are from discharge port 120 discharges simultaneously enter recycling machine 300 along conveyance conduit 200, and the dregs of a decoction discharge thermal energy with the air in heating recovery machine 300, according to The principle that hot-air rises, the air after heating discharge from the gas outlet 321 at 300 top of recycling machine, hot-air and solvent tank Heat exchange type occurs in the first heat exchanger 400 for the cold cut matchmaker of 500 outputs at thermosol matchmaker, and it is defeated that thermosol matchmaker passes through inlet 110 again Enter extract equipment 100, thus realize the recycling of dregs of a decoction thermal energy, with energy saving, and it is anti-compared to being improved in extract equipment 100 The scheme of temperature is answered, the production efficiency for directly adding thermosol matchmaker to extract equipment 100 is higher.
It for protection environment, economizes on resources, the first heat exchanger 400 is also connected with the second heat exchanger 600, solvent receiving tank in turn 700, and coolant liquid, by the second heat exchanger 600, the hot gas that gas outlet 321 discharges is after the output of the first heat exchanger 400, then conveys Heat exchange occurs to the second heat exchanger 600 and with coolant liquid, solvent is precipitated after hot gas condensation, the solvent of condensation is connect by solvent It is stored by tank 700.
Since hot gas is in the first heat exchanger 400 and after cold cut matchmaker's heat exchange, certain temperature is still kept, in gas still It is mixed with the solvent of vaporization, directly externally discharge be easy to cause air pollution, passes through the second heat exchanger 400 of setting and solvent receiving tank 600, which is cooled down, so that solvent liquefaction is precipitated and carries out recycling storage again, so that polluted gas be effectively reduced Discharge and economize on resources.
It is additionally provided with filter device in solvent receiving tank 600, so that the solvent to recycling carries out filter residue, filtrate, so that miscellaneous Mass-energy accesses purification, can be used effectively convenient for solvent after the recovery.
Automatic temperature adjusting valve 800, automatic temperature adjusting valve 800 are additionally provided between first heat exchanger and inlet 110 For controlling the thermosol matchmaker's temperature for entering extract equipment 100, guarantee the production efficiency of extract equipment 100.
To improve heat exchanger effectiveness, the first heat exchanger 400 and the second heat exchanger 600 can be board-like heat exchanger.
In the present embodiment, solvent tank 500 is located at 100 top of extract equipment, and inlet 110 is set to 100 top of extract equipment, Discharge port 120 is set to the bottom of extract equipment 100, to make solvent, the dregs of a decoction be not necessarily to by additional power source, as long as making in gravity It can complete to transport accordingly under, device overall structure is simpler rationally, and manufacturing cost is lower.Preferably, discharge port 120 Tapered setting guides dregs of a decoction discharge by the pyramidal structure of discharge port 120, avoids the dregs of a decoction from remaining in extract equipment 100, out Expect that effect is more preferable.
In the present embodiment, recycling machine 300 can be vertical desolventizing machine.Recycling machine 300 includes casing 310, rotatable turn Column 330, casing 310 have been separated to form at least two reclaiming chambers 320 from top to bottom, have led between two reclaiming chambers 320 of arbitrary neighborhood Material path 323 is connected to, and the reclaiming chamber 320 at top is equipped with gas outlet 321 and feed inlet 322, and rotary column 330 is set in casing 310 The heart and all reclaiming chambers 320 are passed through, the pivoted arm 331 being connected with rotary column 330 is additionally provided in each reclaiming chamber 320, pivoted arm 331 is long Spend super discharge hole 323.
Wherein, pivoted arm 331 can be driven by driving devices such as motors and be rotated, and the dregs of a decoction enter recycling machine by feed inlet 322 300 accommodating chamber, pivoted arm 331 circumferentially rotate under the drive of rotary column 330, and the dregs of a decoction separate after pivoted arm 331 is broken up and from material hole 323 It falls, to accelerate the release of thermal energy, to make full use of the thermal energy in the dregs of a decoction, the dregs of a decoction is avoided to be packed together and heat can not be discharged Amount causes its long-time to contact concurrent heat exchange with casing 310, reduces the formation efficiency of hot-air.Preferably, pivoted arm 331 Bottom surface and side wall respectively close to corresponding reclaiming chamber 320 of bottom surface and side wall, enable pivoted arm 331 that the dregs of a decoction sufficiently to be driven to rotate and make The dregs of a decoction are fallen from material hole 323, and that improves the dregs of a decoction breaks up effect.It is further preferred that the material hole 323 is to lower recess in funnel Shape, the dregs of a decoction can sufficiently fall under the guiding role in funnel-form material hole 323, and the releasing effect of heat is more preferably.
Wherein, it is arranged symmetrically, is had centered on rotary column 330 positioned at the material hole 323 of reclaiming chamber 320 at top, feed inlet 322 Body, the dregs of a decoction under the effect of gravity, the reclaiming chamber 320 at top are entered from the feed inlet 322 of 330 side of rotary column, and the subsequent dregs of a decoction exist It breaks up under the action of pivoted arm 331, and is flowed out after rotating 180 ° from the material hole 323 of 330 other side of rotary column, pass through above-mentioned hole location cloth It sets, before guaranteeing that the dregs of a decoction are fallen from material hole 323, the dregs of a decoction possess sufficiently long rotation distance, and pivoted arm 331 can sufficiently break up medicine Slag, heat releasing effect is more preferably.Preferably, the quantity of reclaiming chamber 320 be five, be connected to reclaiming chamber 320 four material holes 323 with Arrangement is successively rotated by 90 ° under upper centered on rotary column 330, and the dregs of a decoction in the reclaiming chamber 320 at top after falling still with one Fixed heat by the way that multiple reclaiming chambers 320 are arranged, and multiple material holes 323 is set at 90 ° intervals, and the dregs of a decoction is made to carry out multiple beat Day labor sequence guarantees that heat sufficiently discharges, and thermal energy recovering effect is more preferably.
Each reclaiming chamber 320 is correspondingly arranged on hatch door 340.In use, a part of dregs of a decoction are fallen to most under the effect of gravity The reclaiming chamber 320 of bottom, another part remain in reclaiming chamber 320, and the dregs of a decoction remained in reclaiming chamber 320 will affect thermal energy The dregs of a decoction in all reclaiming chambers 320 can very easily be taken out by hatch door 340, guarantee thermal energy recovering effect by recycling.
In addition, the feed inlet 322 of recycling machine 300 is higher than the discharge port 120 of the extract equipment 100, and conveyance conduit 200 It is interior to be equipped with conveying hoister.Existing extract equipment 100 is generally installed on ground by stabilizer blade, and discharge port 120 is also set to and mentions It takes 100 bottom of equipment and close to ground, the dregs of a decoction very easily can be delivered to by recycling by the conveying hoister in delivery pipe The top of machine 300 makes full use of the thermal energy recycling of recycling machine 300 to act on, and discharges the thermal energy of the dregs of a decoction and hot-air rising principle It is adapted, and shortens move distance of the air in recycling machine 300 to reduce the waste of heat, recovering effect is more preferably.Preferably, The outer wall of recycling machine 300 is equipped with thermal insulation layer, to reduce the heat waste of recycling machine 300, improves the thermal energy recycling of recycling machine 300 Efficiency.
The specific embodiments described herein are merely examples of the spirit of the present invention.The utility model institute Belonging to those skilled in the art can make various modifications or additions to the described embodiments or using similar Mode substitute, but without departing from the spirit of the present application or beyond the scope of the appended claims.

Claims (10)

1. a kind of heat-energy recovering apparatus characterized by comprising
Extract equipment is equipped with inlet and discharge port;
Recycling machine, top are equipped with feed inlet and discharge the gas outlet of hot gas, and feed inlet is connected by conveyance conduit with discharge port It is logical;
First Heat Exchanger, one end are connected with gas outlet, and the other end is connected with inlet;
Solvent tank conveys cold cut matchmaker to the first heat exchanger, and cold cut matchmaker is formed after heat exchange occurs with the hot gas that gas outlet discharges Thermosol matchmaker, thermosol matchmaker pass through inlet again and input extract equipment.
2. a kind of heat-energy recovering apparatus according to claim 1, it is characterised in that: first heat exchanger is also sequentially connected There are the second heat exchanger, solvent receiving tank, and coolant liquid, by the second heat exchanger, the hot gas of gas outlet release is defeated from the first heat exchanger It after out, then is delivered to the second heat exchanger and heat exchange occurs with coolant liquid, solvent, the solvent of condensation is precipitated after hot gas condensation It is stored by solvent pans.
3. a kind of heat-energy recovering apparatus according to claim 1, it is characterised in that: first heat exchanger and inlet it Between be provided with automatic temperature adjusting valve.
4. a kind of heat-energy recovering apparatus according to claim 1, it is characterised in that: the recycling machine includes casing, can turn Dynamic rotary column, casing have been separated to form at least two reclaiming chambers from top to bottom, have led to material path between two reclaiming chambers of arbitrary neighborhood Connection, the reclaiming chamber at top are equipped with gas outlet and feed inlet, and rotary column is set to the center of casing and passes through all reclaiming chambers, remove bottom Reclaiming chamber outside, the pivoted arm being connected with rotary column, the super discharge hole of arm length are additionally provided in each reclaiming chamber.
5. a kind of heat-energy recovering apparatus according to claim 4, it is characterised in that: positioned at the reclaiming chamber at top material hole, Feed inlet is arranged symmetrically centered on rotary column.
6. a kind of heat-energy recovering apparatus according to claim 4, it is characterised in that: the quantity of the reclaiming chamber is five, Four material holes for being connected to reclaiming chamber are successively rotated by 90 ° arrangement under upper centered on rotary column.
7. a kind of heat-energy recovering apparatus according to claim 4, it is characterised in that: each reclaiming chamber is correspondingly arranged on cabin Door.
8. a kind of heat-energy recovering apparatus according to claim 1, it is characterised in that: the solvent tank is located in extract equipment Side, inlet are set at the top of extract equipment, and discharge port is set to the bottom of extract equipment.
9. a kind of heat-energy recovering apparatus according to claim 6, it is characterised in that: the tapered setting of discharge port.
10. a kind of heat-energy recovering apparatus according to claim 7, it is characterised in that: the feed inlet of the recycling machine is higher than The discharge port of the extract equipment, and conveying hoister is equipped in conveyance conduit.
CN201821685583.6U 2018-10-17 2018-10-17 A kind of heat-energy recovering apparatus Active CN209188178U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821685583.6U CN209188178U (en) 2018-10-17 2018-10-17 A kind of heat-energy recovering apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821685583.6U CN209188178U (en) 2018-10-17 2018-10-17 A kind of heat-energy recovering apparatus

Publications (1)

Publication Number Publication Date
CN209188178U true CN209188178U (en) 2019-08-02

Family

ID=67408257

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821685583.6U Active CN209188178U (en) 2018-10-17 2018-10-17 A kind of heat-energy recovering apparatus

Country Status (1)

Country Link
CN (1) CN209188178U (en)

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