CN104194636A - Colophony production equipment - Google Patents
Colophony production equipment Download PDFInfo
- Publication number
- CN104194636A CN104194636A CN201410445992.9A CN201410445992A CN104194636A CN 104194636 A CN104194636 A CN 104194636A CN 201410445992 A CN201410445992 A CN 201410445992A CN 104194636 A CN104194636 A CN 104194636A
- Authority
- CN
- China
- Prior art keywords
- fat liquid
- pot
- pipeline
- pan
- water washing
- 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.)
- Granted
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 147
- 239000007788 liquid Substances 0.000 claims abstract description 137
- 238000005406 washing Methods 0.000 claims abstract description 69
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims abstract description 47
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 claims abstract description 47
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 claims abstract description 47
- 238000011084 recovery Methods 0.000 claims abstract description 44
- 238000004065 wastewater treatment Methods 0.000 claims abstract description 26
- 230000007704 transition Effects 0.000 claims abstract description 22
- 238000004821 distillation Methods 0.000 claims abstract description 14
- 238000001816 cooling Methods 0.000 claims description 31
- 239000001293 FEMA 3089 Substances 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 17
- 239000002244 precipitate Substances 0.000 claims description 12
- 239000012530 fluid Substances 0.000 claims description 7
- 238000005452 bending Methods 0.000 claims description 2
- 239000002699 waste material Substances 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 abstract description 4
- 238000004134 energy conservation Methods 0.000 abstract description 2
- 241000779819 Syncarpia glomulifera Species 0.000 abstract 3
- 239000001739 pinus spp. Substances 0.000 abstract 3
- 229940036248 turpentine Drugs 0.000 abstract 3
- 238000009833 condensation Methods 0.000 abstract 1
- 230000005494 condensation Effects 0.000 abstract 1
- 238000001556 precipitation Methods 0.000 abstract 1
- 238000004064 recycling Methods 0.000 abstract 1
- 101150006573 PAN1 gene Proteins 0.000 description 9
- 239000012535 impurity Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000003020 moisturizing effect Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- -1 finally Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Abstract
The invention relates to colophony production equipment which comprises an equipment group and a pipeline group, wherein the equipment group comprises a dissolving pan, a high-order pan, a hot water pan, a rosin liquid washing device, a middle-layer rosin liquid treatment pan, a transition pan, a waste water treatment pan, a rosin liquid precipitation device, a distillation and condensation device, a colophony release groove, a turpentine storage tank, a turpentine recovery pump, a turpentine recycling storage tank and a pipeline cooler; the pipeline group comprises a rosin liquid delivery pipeline, a rosin liquid recovery pipeline, a hot water pipeline, a vapor recovery pipeline and a steam heating pipeline; and all devices of the equipment group are connected through the pipelines of the pipeline group. The colophony production equipment disclosed by the invention has the advantages of reasonability in structure, no middle-layer rosin generation, water conservation, energy conservation and extremely less rosin resource waste.
Description
Technical field
The present invention relates to a kind of rosin production equipment.
Background technology
Existing technology for producing colophony process, has produced a lot of middle levels fat, and middle level fat treating processes is comparatively complicated, causes rosin resource not saved.Due to the limitation of equipment and process, existing rosin production can expend a large amount of heat energy and water resources, owing to not having rational technique can be combined into a large amount of costs with the annual large-scale rosin processing of equipment corresponding with technological process, and waste a large amount of resources, be unfavorable for that China's rosin refines industry.As the rosin of basic resource, if expensive, again can frame the cost of high other products.
Summary of the invention
Goal of the invention of the present invention be to provide a kind of rational in infrastructure, not only produce but also save water and energy without middle level fat, the few rosin production equipment of waste rosin resource.
In order to realize foregoing invention object, the present invention has adopted following technical scheme:
A kind of rosin production equipment, comprises equipment group and pipeline group; Described equipment group comprises that dissolving pan, high-level boiler, water bath, fat liquid water washing device, middle level fat liquid are processed pot, transition pot, wastewater treatment pot, fat liquid precipitate device, distill condensing works, put fragrant groove, storage tank for turpentine oil, turps recovery pump, turps reuse storage tank and tube-cooled device; Pipeline group comprises fat liquid transport pipe, fat liquid recovery channel, hot water pipeline, vapor recovery pipeline and steam-heated pipe line; Described dissolving pan feed liquid output terminal connects high-level boiler top by fat liquid transport pipe, so that dissolving pan minute-pressure send fat liquid to enter high-level boiler; High-level boiler middle part connects fat liquid water washing device by fat liquid transport pipe, and high-level boiler bottom connects middle level fat liquid by fat liquid recovery channel and processes pot; Fat liquid water washing device middle part connects fat liquid precipitate device by fat liquid transport pipe; Fat liquid precipitate device output terminal connects distillation condensing works; Fat liquid water washing device bottom connects middle level fat liquid by fat liquid recovery channel and processes pot bottom; Middle level fat liquid is processed pot top output terminal and is connected successively transition pot and wastewater treatment pot by fat liquid recovery channel; The described transition pot middle part output terminal described dissolving pan that is linked back; Described fat liquid precipitate bottom of device connects wastewater treatment pot by pipeline; The bottom of described distillation condensing works connects puts fragrant groove, and the colling end of distillation condensing works connects storage tank for turpentine oil, and storage tank for turpentine oil connects turps reuse storage tank by turps recovery pump; Described water bath connects respectively dissolving pan, fat liquid water washing device, middle level fat liquid processing pot, transition pot and wastewater treatment pot by hot water pipeline; Described steam-heated pipe line connects respectively dissolving pan, fat liquid precipitate device, distillation condensing works, fat liquid water washing device, middle level fat liquid processing pot and wastewater treatment pot; Described high-level boiler, fat liquid water washing device, middle level fat liquid are processed the input terminus that pot, transition pot, wastewater treatment pot and storage tank for turpentine oil are all connected described hot steam recovery channel, the output terminal connecting tube water cooler of hot steam recovery channel.
As preferably, the fat liquid recovery channel connecting between described transition pot and wastewater treatment pot is to be connected by transition pot top, is connected into wastewater treatment pot top.
As preferably, described distillation condensing works comprises still pot and water cooler; Described still pot top is provided with feed-pipe, and still pot top is connected with cooling tube; Described cooling tube outer end comprises a horizontal cooling pipeline section being made up of the bending of cooling tube body and the downward opening bend loss of an output terminal, and horizontal cooling pipeline section is sealedly connected on described water cooler by the downward opening bend loss of described output terminal; Water cooler bottom connects the top of storage tank for turpentine oil by pipeline.
As preferably, cooling tube is connected in sequence by taper pipeline section, the horizontal cooling pipeline section of bottom, roundabout pipeline section and the downward opening bend loss of output terminal being connected between taper pipeline section and horizontal cooling pipeline section.
Further, also comprise hot water reuse pipe, described horizontal cooling pipeline section outside is arranged with condenser, and described condenser output terminal connects water bath by hot water reuse pipe.
As preferably, described in put fragrant groove top and be provided with capping, described capping top connects the top of storage tank for turpentine oil by pipeline.
As preferably, the connecting tube between described water cooler and storage tank for turpentine oil is provided with turps pipeline buffer, and described turps pipeline buffer top connects vapor recovery pipeline by pipeline.
As preferably, described fat liquid water washing device comprises the first water washing pan and the second water washing pan, and described high-level boiler is connected to the top of the first water washing pan and the top of the second water washing pan by fat liquid transport pipe respectively; Fat liquid transport pipe between high-level boiler and the first water washing pan is provided with the first variable valve, and the first variable valve below is provided with first connecting rod and is arranged on the first pulling part on high-level boiler underframe, and the first variable valve connects the first pulling part of below by first connecting rod; Fat liquid transport pipe between high-level boiler and the second water washing pan is provided with the second variable valve, and the second variable valve below is provided with second connecting rod and is arranged on the second pulling part on high-level boiler underframe, and the second variable valve connects the second pulling part of below by second connecting rod; Described the first pulling part and the second pulling part are nuzzled mutually.
As preferably, described the first water washing pan is identical with the second water washing pan shape, includes a pot body, described pot body and is provided with that fat liquid fluid inlet, hot water fill into mouthful and fat liquid liquid outlet; Described pot body inside bottom is provided with well heater; Also comprise the water mill mechanism being arranged in pot body, described water mill mechanism comprises that upper end is connected to rotating shaft in the external power set of pot, is fixed on the Moving plate of rotating shaft lower end and is fixed on pot quiet dish at body middle part; Described Moving plate is parallel with quiet dish, and upper and lower corresponding and leave water mill gap between Moving plate and quiet dish, the middle part of Moving plate is provided with multiple feed ports, and multiple feed ports are arranged around described rotating shaft.
As preferably, described fat liquid precipitate device comprises the first clarifying kettle, the second clarifying kettle and the 3rd clarifying kettle; Described the first clarifying kettle, the second clarifying kettle and the 3rd clarifying kettle middle part are connected successively, and described the first clarifying kettle, the second clarifying kettle and the 3rd clarifying kettle bottom connect into wastewater treatment pot successively by pipeline.
As preferably, the top of described the first clarifying kettle, the second clarifying kettle, the 3rd clarifying kettle, the first water washing pan and the second water washing pan is all connected vapor recovery pipeline.
The present invention has adopted the rosin production equipment of technique scheme, and by this rosin production equipment, the present invention passes through vapor recovery pipeline, the turps that recovery is easily volatilized and a small amount of water vapor; Is connected with each pot and device in aforesaid device group by fat liquid recovery channel, can multi-layer, effectively process the rosin dissolving, the waste of minimizing rosin resource, the while also reduces heat energy loss.In a word, this rosin production equipment not only make middle level fat in whole technological process processed fall, but also improved efficiency and the effect that whole rosin refines, reduce the waste of water, heat energy and rosin resource.
Brief description of the drawings
Fig. 1: the process flow sheet of rosin production equipment in the embodiment of the present invention.
Fig. 2: in the embodiment of the present invention, rosin production equipment is not connected into the process flow sheet of steam-heated pipe line.
Fig. 3: the sectional perspective structural representation one of rosin production equipment in the embodiment of the present invention.
Fig. 4: the sectional perspective structural representation two of rosin production equipment in the embodiment of the present invention.
Fig. 5: the cross-sectional view of water washing pan in the embodiment of the present invention.
Embodiment
Below in conjunction with accompanying drawing, the present invention is described further.
Embodiment 1: rosin production equipment as shown in Figure 1, Figure 2, Figure 3 and Figure 4, this rosin production equipment comprises equipment group and pipeline group.Wherein:
Equipment group comprises that dissolving pan 1, high-level boiler 2, water bath 3, the first water washing pan 5a, the second water washing pan 5b, middle level fat liquid are processed pot 7, transition pot 8, wastewater treatment pot 9, the first clarifying kettle 6a, the second clarifying kettle 6b, the 3rd clarifying kettle 6c, distill condensing works, put fragrant groove 11, storage tank for turpentine oil 13, turps recovery pump 14, turps reuse storage tank 4 and tube-cooled device 15.
Pipeline group comprises fat liquid transport pipe 21, fat liquid recovery channel 22, hot water pipeline 18, vapor recovery pipeline 20, hot water reuse pipe 17, steam-heated pipe line 19 and the most common pipeline.
Core of the present invention is the mode of connection of equipment group and pipeline group and technical process to adjust, and makes rosin equipment provided by the present invention not only without middle level fat, and reclaims better turps, water saving, energy-conservation, saving rosin resource.Its concrete structure and annexation are as follows:
Dissolving pan 1 feed liquid output terminal connects high-level boiler 2 tops by fat liquid transport pipe 21, on dissolving pan 1 is interior, adds rosin raw material, and steam-heated pipe line 19 passes into steam direct heating, makes rosin become translucent fluid, and its water content is between 10-20%.Deviate from impurity in dissolving pan 1 bottom, as dust, leaf and sand, on dissolving pan 1 top, form the minute-pressure of 0.45Mpa, fat liquid less impurity is entered to high-level boiler 2.
High-level boiler 2 belows are provided with underframe, the output terminal of high-level boiler 2 is divided into multilayer, wherein high-level boiler 2 tops are connected into vapor recovery pipeline 20, its middle part connects respectively the top of the first water washing pan 5a and the top of the second water washing pan 5b by fat liquid transport pipe 21, and high-level boiler 2 bottoms connect the top of middle level fat liquid processing pot 7 by fat liquid recovery channel 22.Fat liquid transport pipe 21 between high-level boiler 2 and the first water washing pan 5a is provided with the first variable valve 21a, the first pulling part 211, the first variable valve 21a that are provided with first connecting rod 210a below the first variable valve 21a and be arranged on high-level boiler 2 underframe pass through the first pulling part 211 that first connecting rod 210a connects below.Fat liquid transport pipe 21 between high-level boiler 2 and the second water washing pan 5b is provided with the second variable valve 21b, the second pulling part 212, the second variable valve that are provided with second connecting rod 210b below the second variable valve 21b and be arranged on high-level boiler 2 underframe pass through the second pulling part 212 that second connecting rod 210b connects below; Described the first pulling part 211 and the second pulling part 212 are nuzzled mutually.Connecting rod and pulling part mode of connection are adopted, the lowerd work point of the first variable valve 21a and the second variable valve 21b, make its operator in actually operating easy to operate, be convenient to adjust respectively the liquid level between the first water washing pan 5a and the second water washing pan 5b, make whole water washing process continuous.
The bottom of above-mentioned the first water washing pan 5a and the second water washing pan 5b is all connected into the bottom of middle level fat liquid processing pot 7 by fat liquid recovery channel 22, i.e. middle level fat liquid processing pot 7 receives respectively the fat liquid input of high-level boiler 2 bottoms and first, second water washing pan 5a, 5b from upper and lower.Because the fat liquid of high-level boiler 2 bottoms is not washed, impurity percentage composition is less than the fat liquid of washing after washing pot bottom, therefore process between pot 7 upper and lowers and be provided with silk screen at middle level fat liquid, the fat liquid of first, second water washing pan 5a, 5b bottom is squeezed into middle level fat liquid from silk screen below and is processed pot 7, middle level fat liquid is processed pot 7 existing hot water and is carried out moisturizing, there is again steam to heat, the middle level fat liquid of above-mentioned input is heat-treated.Middle level fat liquid is processed the top of pot 7 outputs at middle level fat liquid processing pot 7, its by fat liquid after treatment by being pressed into transition pot 8, there is described dissolving pan 1 output terminal that is linked back at transition pot 8 middle parts, in addition, transition pot 8 also has another output terminal to connect wastewater treatment pot 9, this output, at transition pot 8 tops, mainly exports liquid larger water content to wastewater treatment pot 9.
Above-mentioned water bath 3 connects respectively dissolving pan 1, the first water washing pan 5a, the second water washing pan 5b, middle level fat liquid processing pot 7, transition pot 8 and wastewater treatment pot 9 by hot water pipeline 18, and each pot is carried out to direct hot water heating, carries out moisturizing simultaneously.
The output terminal at above-mentioned the first water washing pan 5a and the second water washing pan 5b middle part is all connected into the first clarifying kettle 6a, and the first clarifying kettle 6a, the second clarifying kettle 6b are connected successively with the 3rd clarifying kettle 6c middle part; The first clarifying kettle 6a, the second clarifying kettle 6b and the 3rd clarifying kettle 6c bottom all connect into wastewater treatment pot 9 successively by pipeline.The output terminal of the 3rd clarifying kettle 6c connects the input terminus of distillation condensing works.
Introduce from outside in steam heating of the present invention source, and separating many steam-heated pipe lines 19 by sub-cylinder 16, steam-heated pipe line 19 output terminals connect respectively dissolving pan 1, the first clarifying kettle 6a, the second clarifying kettle 6b, the 3rd clarifying kettle 6c, distillation condensing works, the first water washing pan 5a, the second water washing pan 5b, middle level fat liquid processing pot 7 and wastewater treatment pot 9.
Above-mentioned distillation condensing works comprises still pot 10 and water cooler 12.Wherein still pot 10 tops are provided with feed-pipe, and still pot 10 bottoms are connected and put fragrant groove 11 by pipeline, and still pot 10 tops are connected with cooling tube.The fat liquid that still pot 10 is sent into the 3rd clarifying kettle 6c to feed-pipe distills, and still pot 10 is interior steams turps and water vapor mixture body, and what still pot 10 bottoms stayed is rosin, and the discharge of pipes by bottom is to putting fragrant groove 11.The cooling tube at still pot 10 tops is specifically connected in sequence by taper pipeline section 101, the horizontal cooling pipeline section 102 of bottom, roundabout pipeline section 1010 and the downward opening bend loss 103 of output terminal being connected between taper pipeline section 101 and horizontal cooling pipeline section 102.10 pots of tops of still pot that taper pipeline section 101 lower ends connect, taper pipeline section 101 upper ends by roundabout pipeline section 1010 convert opening towards, it is docked with horizontal cooling pipeline section 102 smoothly, and make a lot of gases in still pot 10 be liquefied and flow back at roundabout pipeline section 1010, after circulating and evaporating, efficiency and purity are higher.It is cooling that vaporization turps and water vapor carry out one-level at horizontal cooling pipeline section 102.For better cooling, horizontal cooling pipeline section 102 outsides are wherein arranged with condenser 1020, and condenser 1020 is inputted cold water, and its output terminal is provided with hot water reuse pipe 17.Hot water reuse pipe 17 in the present invention, for connecting water bath of the present invention, carries out thermal compensation, reuse heat energy better to the hot water in water bath.After one-level is cooling, the output terminal of above-mentioned horizontal cooling pipeline section 102 is connected on described water cooler 12 by downward opening bend loss 103 water seals of an output terminal, makes turps of the present invention carry out secondary cooling.Water cooler 12 is high-order to be arranged, its bottom connects storage tank for turpentine oil 13 by pipeline, on the connecting tube between water cooler 12 and storage tank for turpentine oil 13, be provided with turps pipeline buffer 120, one of its object be convenient to cushion terebinthine dirty, two be to be convenient to relief pressure in pipeline, and then be convenient to the evaporation of gas, accelerate cooling.The pipeline of above-mentioned water cooler 12 belows is connected into the top of storage tank for turpentine oil 13, turps recovery pump 14 junctions are passed through at high-order turps reuse storage tank 4 in storage tank for turpentine oil 13 bottoms, turps recovery pump 4 is beaten turps to set high position, turps reuse storage tank 4 connects dissolving pan, high-order turps reuse storage tank 4 is also convenient to the equipment in turps add-back dissolution process, rationally reuse turps, reduces the rosin wasting of resources.
In order to reclaim the turps and a small amount of water vapor that easily evaporate, fragrant groove 11 tops of putting in the present invention are provided with capping, and described capping top connects the top of storage tank for turpentine oil 13 by pipeline.Storage tank for turpentine oil 13 tops in the present invention are provided with vapor recovery pipeline 20, turps pipeline buffer 120 tops also connect vapor recovery pipeline 20 by pipeline, in addition, above-mentioned dissolving pan 1, high-level boiler 2, middle level fat liquid is processed pot 7, transition pot 8, wastewater treatment pot 9, the first water washing pan 2, the second water washing pan 3, the first clarifying kettle 6a and the second clarifying kettle 6b, the top of the 3rd clarifying kettle 6c also all connects vapor recovery pipeline 20, vapor recovery pipeline 20 connecting tube of end road water coolers 15, tube-cooled device 15 output terminals are provided with return water pipe 150, by the reasonable reuse of these pure turps.Tube-cooled device 15 of the present invention is spiral riser water coolers.And the present invention above-mentioned are interchanger for the cooling water cooler 12 of secondary.
As shown in Figure 5, above-mentioned the first water washing pan 5a and the second water washing pan 5b all adopt the water washing pan of following structure: this water washing pan is made up of pot body 51, underframe and water mill mechanism, and pot body 51 is fixed on underframe, and water mill mechanism is arranged in pot body 51.
Above-mentioned water mill mechanism specifically comprises that upper end is connected to rotating shaft 520 on pot body 51 outer power devices, is fixed on the Moving plate 521 of rotating shaft 520 lower ends and is fixed on the quiet dish 523 at pot body 51 middle parts, Moving plate 521 and quiet dish 523 are all rounded, coaxial and be arranged in parallel, upper and lower corresponding and leave water mill gap 522 between Moving plate 521 and quiet dish 523, the middle part of Moving plate 521 is provided with multiple feed ports 5210, multiple feed ports 5210 are arranged around described rotating shaft 520, ringwise.Power set wherein can be specifically motor or motor and step-down gear matching mechanism, the mechanism that can be convenient to drive shaft 520 and drive Moving plate 521 high speed rotating that also those skilled in the art commonly use arbitrarily.
Wherein, pot body 51 is provided with fat liquid fluid inlet 510, hot water fills into mouth 511, fat liquid recovery mouth and fat liquid liquid outlet 514.Fat liquid fluid inlet 510 is positioned at described pot body 51 tops, and fat liquid transport pipe 21 docks with it, higher than the residing level attitude of Moving plate 521; Fat liquid liquid outlet 514, hot water fill into mouth 511 and fat liquid fluid inlet 510 is all in a pot side portion, wherein the position of fat liquid liquid outlet 514 is lower than fat liquid fluid inlet 510, be positioned at the residing level attitude of Moving plate 521 but be not less than, fat liquid liquid outlet 514 connects fat liquid transport pipe 21, and fat liquid recovery mouth is in pot body 51 bottoms, hot water fills into mouth 511 and docks with above-mentioned hot water pipeline 18.Pot body 51 inside bottom are provided with well heater, and above-mentioned well heater 512 is vapor heat exchangers, and vapor heat exchanger input terminus connects the heat in pot body 51 outsides and steams input tube 5120, and output terminal connects the coolant outlet hose 5121 in pot body 51 outsides.Vapor heat exchanger is connected into and gives heat supply by being connected into above-mentioned steam-heated pipe line 19.
In order to obtain better washing effect, heater locations is preferably in quiet dish 523 belows, and it is roughly corresponding between Moving plate 521 and quiet dish 523 that the hot water here fills into mouthful 511 positions, and the hot water adding just can be fast by well heater.
Adopt the water washing pan of said structure, by Moving plate 521 and the quiet dish 523 in water washing pan is set, Moving plate 521 high speed rotating make fat liquid in the water mill gap between Moving plate 521 and quiet dish 523 by speed lapping.After fat liquid and water fully mix, water molecules penetrates into around very thin fat liquid particulate, form milky white liquid, thereby the less impurity particle of being convenient in fat liquid is separated.Moving plate 521 middle parts are provided with multiple feed ports 5210, and the Moving plate 521 of high speed rotating makes formation negative pressure in water mill gap after throwing away milky white liquid, and then feed port 5210 can suck untreated fat liquid, finally, water washing pan is continuously washed fat liquid, it is fully mixed with water and break up rosin particle, thus effective removing foreign matter.
Above-described embodiment is only one of the present invention to be described for example, protection scope of the present invention is not restricted, and does similar amendment, converts and be equal to alternative according to the present invention's spirit principle, all falls into protection scope of the present invention.
Claims (10)
1. a rosin production equipment, is characterized in that: comprise equipment group and pipeline group; Described equipment group comprises that dissolving pan (1), high-level boiler (2), water bath (3), fat liquid water washing device, middle level fat liquid are processed pot (7), transition pot (8), wastewater treatment pot (9), a fat liquid precipitate device, distill condensing works, put fragrant groove (11), storage tank for turpentine oil (13), turps recovery pump (14), turps reuse storage tank (4) and tube-cooled device (15); Pipeline group comprises fat liquid transport pipe (21), fat liquid recovery channel (22), hot water pipeline (18), vapor recovery pipeline (20) and steam-heated pipe line (19); Described dissolving pan (1) feed liquid output terminal connects high-level boiler (2) top by fat liquid transport pipe (21), so that dissolving pan (1) minute-pressure send fat liquid to enter high-level boiler (2); High-level boiler (2) middle part connects fat liquid water washing device by fat liquid transport pipe (21), and high-level boiler (2) bottom connects middle level fat liquid by fat liquid recovery channel (22) and processes pot (7); Fat liquid water washing device middle part connects fat liquid precipitate device by fat liquid transport pipe (21); Fat liquid precipitate device output terminal connects distillation condensing works; Fat liquid water washing device bottom connects middle level fat liquid by fat liquid recovery channel (22) and processes pot (7) bottom; Middle level fat liquid is processed pot (7) top output terminal and is connected successively transition pot (8) and wastewater treatment pot (9) by fat liquid recovery channel (22); Described transition pot (8) the top output terminal described dissolving pan (1) that is linked back; Described fat liquid precipitate bottom of device connects wastewater treatment pot (9) by pipeline; The bottom of described distillation condensing works connects puts fragrant groove (11), the colling end of distillation condensing works connects storage tank for turpentine oil (13), and storage tank for turpentine oil (13) connects turps reuse storage tank (4) by turps recovery pump (14); Described water bath (3) connects respectively dissolving pan (1), fat liquid water washing device, middle level fat liquid processing pot (7), transition pot (8) and wastewater treatment pot (9) by hot water pipeline (18); Described steam-heated pipe line (19) connects respectively dissolving pan (1), fat liquid precipitate device, distillation condensing works, fat liquid water washing device, middle level fat liquid processing pot (7) and a wastewater treatment pot (9); Described high-level boiler (2), fat liquid water washing device, middle level fat liquid are processed the input terminus that pot (7), transition pot (8), wastewater treatment pot (9) and storage tank for turpentine oil (13) are all connected described hot steam recovery channel (20), the output terminal connecting tube water cooler (15) of hot steam recovery channel (20).
2. a kind of rosin production equipment according to claim 1, it is characterized in that: the fat liquid recovery channel (22) connecting between described transition pot (8) and wastewater treatment pot (9) is to be connected by transition pot (8) top, is connected into wastewater treatment pot (9) top.
3. a kind of rosin production equipment according to claim 1, is characterized in that: described distillation condensing works comprises still pot (10) and water cooler (12); Described still pot (10) top is provided with feed-pipe, and still pot (1) top is connected with cooling tube; Described cooling tube outer end comprises the horizontal cooling pipeline section (102) being made up of the bending of cooling tube body and the downward opening bend loss of an output terminal (103), and horizontal cooling pipeline section (102) is sealedly connected on described water cooler (12) by the downward opening bend loss of described output terminal (103); Water cooler (12) bottom connects the top of storage tank for turpentine oil (13) by pipeline.
4. a kind of rosin production equipment according to claim 1, is characterized in that: cooling tube is connected in sequence by taper pipeline section (101), the horizontal cooling pipeline section (102) of bottom, roundabout pipeline section (1010) and the downward opening bend loss of output terminal (103) being connected between taper pipeline section (101) and horizontal cooling pipeline section (102).
5. a kind of rosin production equipment according to claim 1, it is characterized in that: also comprise hot water reuse pipe (17), described horizontal cooling pipeline section (14) outside is arranged with condenser (1020), and described condenser (1020) output terminal connects water bath (3) by hot water reuse pipe (17).
6. a kind of rosin production equipment according to claim 1, it is characterized in that: the connecting tube between described water cooler (12) and storage tank for turpentine oil (13) is provided with turps pipeline buffer (120), described turps pipeline buffer (120) top connects vapor recovery pipeline (20) by pipeline; Described fragrant groove (11) top of putting is provided with capping, and described capping top connects the top of storage tank for turpentine oil (13) by pipeline.
7. a kind of rosin production equipment according to claim 1, it is characterized in that: described fat liquid water washing device comprises the first water washing pan (5a) and the second water washing pan (5b), described high-level boiler (2) is connected to the top of the first water washing pan (5a) and the top of the second water washing pan (5b) by fat liquid transport pipe (21) respectively; Fat liquid transport pipe (21) between high-level boiler (2) and the first water washing pan (5a) is provided with the first variable valve (21a), the first variable valve (21a) below is provided with first connecting rod (210a) and is arranged on the first pulling part (211) on high-level boiler (2) underframe, and the first variable valve (21a) connects first pulling part (211) of below by first connecting rod (210a); Fat liquid transport pipe (21) between high-level boiler (2) and the second water washing pan (5b) is provided with the second variable valve (21b), the second variable valve (21b) below is provided with second connecting rod (210b) and is arranged on the second pulling part (212) on high-level boiler (2) underframe, and the second variable valve connects second pulling part (212) of below by second connecting rod (210b); Described the first pulling part (211) and the second pulling part (212) are nuzzled mutually.
8. a kind of rosin production equipment according to claim 7, it is characterized in that: described the first water washing pan (5a) is identical with the second water washing pan (5b) shape, include that a pot body (51), described pot body (51) are provided with fat liquid fluid inlet (510), hot water fills into mouthful (511) and a fat liquid liquid outlet (514); Described pot body (51) inside bottom is provided with well heater; Also comprise the water mill mechanism being arranged in a pot body (51), described water mill mechanism comprises that upper end is connected to rotating shaft (520) on a pot body (51) outer power device, is fixed on the Moving plate (521) of rotating shaft (520) lower end and is fixed on the quiet dish (523) at a pot body (51) middle part; Described Moving plate (521) is parallel with quiet dish (523), upper and lower corresponding and leave water mill gap (522) between Moving plate (521) and quiet dish (523), the middle part of Moving plate (521) is provided with multiple feed ports (5210), and multiple feed ports (5210) are arranged around described rotating shaft (520).
9. a kind of rosin production equipment according to claim 1, is characterized in that: described fat liquid precipitate device comprises the first clarifying kettle (6a), the second clarifying kettle (6b) and the 3rd clarifying kettle (6c); Described the first clarifying kettle (6a), the second clarifying kettle (6b) and the 3rd clarifying kettle (6c) middle part are connected successively, and described the first clarifying kettle (6a), the second clarifying kettle (6b) and the 3rd clarifying kettle (6c) bottom connect into wastewater treatment pot (9) successively by pipeline.
10. a kind of rosin production equipment according to claim 9, is characterized in that: described the first clarifying kettle (6a), the second clarifying kettle (6b), the 3rd clarifying kettle (6c), the first water washing pan (2) are all connected vapor recovery pipeline (20) with the top of the second water washing pan (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410445992.9A CN104194636B (en) | 2014-09-03 | 2014-09-03 | A kind of rosin production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410445992.9A CN104194636B (en) | 2014-09-03 | 2014-09-03 | A kind of rosin production equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104194636A true CN104194636A (en) | 2014-12-10 |
| CN104194636B CN104194636B (en) | 2015-10-28 |
Family
ID=52080014
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410445992.9A Active CN104194636B (en) | 2014-09-03 | 2014-09-03 | A kind of rosin production equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104194636B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106634613A (en) * | 2016-12-26 | 2017-05-10 | 景谷兴发林化有限公司 | Continuous production system for rosin |
| CN106675415A (en) * | 2016-12-22 | 2017-05-17 | 临沧方源林产品有限公司 | Rosin production and processing system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102286250A (en) * | 2011-07-07 | 2011-12-21 | 江西飞尚林产有限公司 | Method for processing primary rosin by middle layer grease liquid |
| CN202658123U (en) * | 2012-04-24 | 2013-01-09 | 桂林兴松林化有限责任公司 | High-efficiency, energy-saving, low-cost and high-quality rosin production line equipment |
| CN203065385U (en) * | 2013-01-21 | 2013-07-17 | 云南茶花林化有限公司 | Rosin processing system |
| CN204111647U (en) * | 2014-09-03 | 2015-01-21 | 松阳县永新机械制造有限公司 | Rosin production equipment |
-
2014
- 2014-09-03 CN CN201410445992.9A patent/CN104194636B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102286250A (en) * | 2011-07-07 | 2011-12-21 | 江西飞尚林产有限公司 | Method for processing primary rosin by middle layer grease liquid |
| CN202658123U (en) * | 2012-04-24 | 2013-01-09 | 桂林兴松林化有限责任公司 | High-efficiency, energy-saving, low-cost and high-quality rosin production line equipment |
| CN203065385U (en) * | 2013-01-21 | 2013-07-17 | 云南茶花林化有限公司 | Rosin processing system |
| CN204111647U (en) * | 2014-09-03 | 2015-01-21 | 松阳县永新机械制造有限公司 | Rosin production equipment |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106675415A (en) * | 2016-12-22 | 2017-05-17 | 临沧方源林产品有限公司 | Rosin production and processing system |
| CN106675415B (en) * | 2016-12-22 | 2023-06-23 | 临沧方源林产品有限公司 | Rosin production system of processing |
| CN106634613A (en) * | 2016-12-26 | 2017-05-10 | 景谷兴发林化有限公司 | Continuous production system for rosin |
| CN106634613B (en) * | 2016-12-26 | 2019-11-19 | 景谷兴发林化有限公司 | Rosin continuous process system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104194636B (en) | 2015-10-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101935077B (en) | Waste acid concentration multistage treatment method | |
| CN204034294U (en) | The board-like forced-circulation evaporator of novel triple effect | |
| CN204034286U (en) | Board-like mechanical vapour recompression evaporator | |
| CN201030243Y (en) | Vapor-recompression energy-conservation evaporator | |
| CN206304378U (en) | The energy-conservation MVR evaporators that a kind of vapor recompression is utilized | |
| CN103073141B (en) | Low-temperature multi-effect distilled seawater desalination system with variable effect groups | |
| CN206902054U (en) | DMAC recovery systems | |
| CN102226130B (en) | Tea tree oil extractor | |
| CN104524793A (en) | MVR evaporator | |
| CN104194636B (en) | A kind of rosin production equipment | |
| CN206705724U (en) | A kind of environmental protection and energy saving waste water distilling apparatus | |
| CN201519474U (en) | External circulating evaporator | |
| CN101825360A (en) | Method and device for recycling high-pressure dissolved steam exhaust of diluting tank in alumina production | |
| CN106439784B (en) | A kind of full-automatic deaerator exhaust heat energy recycle method and its system | |
| CN204111647U (en) | Rosin production equipment | |
| CN104231939B (en) | A kind of rosin production method | |
| CN204380287U (en) | A kind of MVR evaporimeter | |
| CN103182194A (en) | Integrated-type liquid vaporization-separation tank device | |
| CN104606910A (en) | Heat pump rectifying device based on heat storage technology and starting method of heat pump rectifying device | |
| CN205227896U (en) | Condensate water is recovery system again | |
| CN102698450A (en) | Two-stage falling-climbing film evaporator | |
| CN109019725A (en) | A kind of energy conservation water vaporization tower | |
| CN204170435U (en) | Energy-saving board-like mechanical vapour recompression evaporator | |
| CN205917031U (en) | Phosphoric acid refrigeration cycle water vacuum device | |
| CN209423190U (en) | A kind of new and effective automatically cleaning super heat-conductive pipe takes off white device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190528 Address after: 530007 Peace Village, Nachen Town, Liangqing District, Nanning City, Guangxi Zhuang Autonomous Region Patentee after: Nanning Heping rosin factory Address before: 530004 Science and Technology Building 1122, 27 Keyuan Avenue, Xixiangtang District, Nanning City, Guangxi Zhuang Autonomous Region Patentee before: Guangxi Xuanmao Technology Co.,Ltd. Effective date of registration: 20190528 Address after: 530004 Science and Technology Building 1122, 27 Keyuan Avenue, Xixiangtang District, Nanning City, Guangxi Zhuang Autonomous Region Patentee after: Guangxi Xuanmao Technology Co.,Ltd. Address before: 323400 No. 10 Changhong East Road, Xiping Street, Songyang County, Lishui City, Zhejiang Province Patentee before: SONGYANG YONGXIN MACHINERY MANUFACTURING Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190710 Address after: 530007 Peace Village, Nachen Town, Liangqing District, Nanning City, Guangxi Zhuang Autonomous Region Patentee after: Nanning Heping rosin factory Address before: 530004 Science and Technology Building 1122, 27 Keyuan Avenue, Xixiangtang District, Nanning City, Guangxi Zhuang Autonomous Region Patentee before: Guangxi Xuanmao Technology Co.,Ltd. Effective date of registration: 20190710 Address after: 530004 Science and Technology Building 1122, 27 Keyuan Avenue, Xixiangtang District, Nanning City, Guangxi Zhuang Autonomous Region Patentee after: Guangxi Xuanmao Technology Co.,Ltd. Address before: 323400 No. 10 Changhong East Road, Xiping Street, Songyang County, Lishui City, Zhejiang Province Patentee before: SONGYANG YONGXIN MACHINERY MANUFACTURING Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210316 Address after: 223800 No.2, building a, Jinhua Mingyuan, Suyu District, Suqian City, Jiangsu Province Patentee after: Jiangsu ruishengda Construction Engineering Co.,Ltd. Address before: 530007 Heping Village, nachen Town, Liangqing District, Guangxi Zhuang Autonomous Region Patentee before: Nanning Heping rosin factory |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210420 Address after: 223900 No.17 Hengshan North Road, Sihong Economic Development Zone, Suqian City, Jiangsu Province Patentee after: Jiangsu Huayong Construction Engineering Co.,Ltd. Address before: 223800 No.2, building a, Jinhua Mingyuan, Suyu District, Suqian City, Jiangsu Province Patentee before: Jiangsu ruishengda Construction Engineering Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210625 Address after: 223900 A20, building 2, agricultural machinery market, Sihong County, Suqian City, Jiangsu Province Patentee after: Jiangsu Hongjin Construction Co.,Ltd. Address before: 223900 No.17 Hengshan North Road, Sihong Economic Development Zone, Suqian City, Jiangsu Province Patentee before: Jiangsu Huayong Construction Engineering Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210913 Address after: No.62, new street, Hankou village, Dapu Town, Yongchun County, Quanzhou City, Fujian Province 362600 Patentee after: Xu Xiaodong Address before: 223900 A20, building 2, agricultural machinery market, Sihong County, Suqian City, Jiangsu Province Patentee before: Jiangsu Hongjin Construction Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20211008 Address after: Liu'an Development Zone, Yongchun County, Quanzhou City, Fujian Province (east side of Taoxi bridge) Patentee after: Yongchun County Product Quality Inspection Institute Fujian fragrance product quality inspection center, national incense burning product quality supervision and Inspection Center (Fujian) Address before: No.62, new street, Hankou village, Dapu Town, Yongchun County, Quanzhou City, Fujian Province 362600 Patentee before: Xu Xiaodong |
|
| TR01 | Transfer of patent right |