CN106861544A - A kind of full-closed zero discharge continuous prodution modified pitch device and method - Google Patents

A kind of full-closed zero discharge continuous prodution modified pitch device and method Download PDF

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Publication number
CN106861544A
CN106861544A CN201710143294.7A CN201710143294A CN106861544A CN 106861544 A CN106861544 A CN 106861544A CN 201710143294 A CN201710143294 A CN 201710143294A CN 106861544 A CN106861544 A CN 106861544A
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machine
modified pitch
pitch
bitumenpump
sbs
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CN201710143294.7A
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CN106861544B (en
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李振华
李滢
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/82Combinations of dissimilar mixers
    • B01F33/821Combinations of dissimilar mixers with consecutive receptacles
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L95/00Compositions of bituminous materials, e.g. asphalt, tar, pitch
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/38Mixing of asphalt, bitumen, tar or pitch or their ingredients
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/30Adapting or protecting infrastructure or their operation in transportation, e.g. on roads, waterways or railways
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Abstract

The invention belongs to ground surface material technical field, specially a kind of device and method of full-closed zero discharge continuous prodution modified pitch.The process units is made up of bitumenpump, forced feed machine, reciprocating single screw rod mixing machine, single-stage high-shear emulsion machine, combined static blender, multi-stage high shear mulser through pipeline connection.By controlling temperature, the rotating speed etc. of individual device, the production of full-closed zero discharge serialization SBS modified pitch is realized.The present invention changes traditional SBS Production Process of Modified Bitumen, and from the matrix pitch from storage tank to the qualified SBS modified pitch of output, production process is totally-enclosed, does not have any waste gas discharge;Process route is concise; it is simple to operate; floor space is small; it is very convenient supporting with bitumen concrete mixing station; accomplish with the startup-shutdown production simultaneously of bitumen concrete mixing station, it is necessary to how many SBS modified pitch just produce how much, reduce the multiple transport of pitch and modified pitch and heat influence to modified pitch quality repeatedly; it is simultaneously energy-saving, it is cost-effective.

Description

A kind of full-closed zero discharge continuous prodution modified pitch device and method
Technical field
The invention belongs to ground surface material technical field, and in particular to a kind of full-closed zero discharge continuous prodution modified pitch Device and method.
Background technology
It is right as the trend on China's road construction " high-quality road ", " environment-friendlyroad road ", " ecological road ", " characteristic road " is increased rapidly The performance of asphalt pavement material proposes requirement higher, to asphalt pavement material production system and asphalt pavement construction operation Energy-conserving and environment-protective it is also proposed requirement higher.
In order to adapt to the demand in pavement material market, SBS modified pitch, SBS asphaltum with high viscosity, rubber powder modified asphalt, coloured silk All kinds of modified pitch such as color pitch, warm-mixed asphalt are more and more applied, and are allowed to produce the process units of modified pitch, Increased rapidly.However, current modified asphalt production device, is produced using pot type gap method, technology controlling and process temperature Degree is all controlled more than 175 DEG C, is not only consumed energy big, and smoke pollution is serious, can also cause the aging of modified pitch, influences product matter Amount.And it is current, reply modified pitch produces waste gas also not effectively eliminate measure when producing and paving.
The content of the invention
It is an object of the present invention to provide a kind of device and method of full-closed zero discharge continuous prodution modified pitch.
The device of the full-closed zero discharge continuous prodution modified pitch that the present invention is provided, its structure and process chart are such as Shown in Fig. 1.The device is by three bitumenpumps, forced feed machine, a reciprocating spiral mixing machine, a single-stage high shear Mulser, a combined static blender, a multi-stage high shear mulser and according to technological requirement connect above equipment Pipeline composition;Wherein, bitumenpump 1, forced feed machine 2 connect reciprocating spiral mixing machine 3, reciprocating spiral mixing machine respectively After 3 connection single-stage high-shear emulsion machines 4, be sequentially connected bitumenpump 5, combined static blender 6, multi-stage high shear mulser 7, Bitumenpump 8.The outlet of bitumenpump 8 connects modified pitch storage tank or bitumen concrete mixing station by pipeline.
In the present invention, the single-stage high-shear emulsion machine and multi-stage high shear mulser can use functionally similar colloid mill Substitute.
The device of the full-closed zero discharge continuous prodution modified pitch that the present invention is provided, produces the specific stream of modified pitch Journey is as follows:110 DEG C -150 DEG C of matrix pitch temperature from storage tank, by the first bitumenpump(1)Input reciprocating spiral mix Machine(3), meanwhile, the SBS and the compound of additive being pre-mixed in proportion, by forced feed machine(2)Add reciprocating Spiral mixing machine(3);The mixed material of SBS and additive, in reciprocating spiral mixing machine(3)It is interior mix with matrix pitch after, It is continuous uninterrupted into single-stage high-shear emulsion machine(4)In, preliminary dispersion, shearing, then by the second bitumenpump(5)It is input to group Box-like static mixer(6)Be stirred, mix, it is swelling, subsequently into multi-stage high shear mulser(7), finally by the 3rd drip Blue or green pump(8)Input storage tank or bitumen concrete mixing station.Realize the purpose of full-closed zero discharge continuous prodution SBS modified pitch.
The composition of SBS of the present invention and additive formulations is(By weight):
Matrix pitch 80-90 parts;
SBS 2-7 parts;
Additive:Aromatic naphtha or machine oil 4-10 parts;
Additive:Microwax and/or stearic acid 3-10 parts.
Further, in process of production, suitable additive is selected, operation temperature, saving energy consumption can be further reduced. For example, if additive uses aromatic naphtha and microwax, operation temperature is controlled at 160 DEG C -180 DEG C in addition to forced feed machine; At this moment matrix pitch temperature is preferably 120 DEG C -150 DEG C.If additive uses machine oil, and microwax and stearic acid, operation temperature Degree is controlled at 130 DEG C -150 DEG C in addition to forced feed machine;At this moment matrix pitch temperature is preferably 110 DEG C -130 DEG C.
It can be seen that, when additive is machine oil and microwax and stearic acid, the operation temperature of production process can be made to change than conventional Property 25 DEG C -35 DEG C of asphalt production process reduction, the modified pitch of production can also reduce by 25 DEG C of bitumen concrete mix decking and rolling temperature - 35 DEG C, further energy-saving and emission-reduction.
In the present invention, conduction oil that the control of operation temperature can be configured by present device and its relevant connection pipeline or Electric heating automatic control system is realized.
The device and method of full-closed zero discharge continuous prodution modified pitch of the invention, changes traditional SBS and is modified The technique of asphalt production, from the pitch from storage tank to the qualified SBS modified pitch of output, production process is totally-enclosed, no to appoint What waste gas discharge.Process route is concise, simple to operate simultaneously, and floor space is small, very convenient supporting with bitumen concrete mixing station, does To with bitumen concrete mixing station simultaneously startup-shutdown production, it is necessary to how many SBS modified pitch just produce how much, reduce pitch or product Multiple transport and heat influence to product quality repeatedly, it is cost-effective while energy-saving.
Brief description of the drawings
Fig. 1 is the process chart of the device and method of full-closed zero discharge continuous prodution modified pitch of the invention.
Label in figure:1 is bitumenpump, and 2 is forced feed machine, and 3 is reciprocating spiral mixing machine, and 4 is single-stage high shear breast Change machine, 5 is bitumenpump, and 6 is combined static blender, and 7 is multi-stage high shear mulser, and 8 is bitumenpump.
Specific embodiment
The modified asphalt production device that the present invention is provided, capital equipment is:Three bitumenpumps, forced feed machine is reciprocating Spiral mixing machine, single-stage high-shear emulsion machine, combined static blender, multi-stage high shear mulser.
Capital equipment and its function:
1. three bitumenpumps 1,5,8, are the screw rod bitumenpump with heating and heat insulation function purchased in market.Main Function is conveying base Matter pitch and modified pitch.
2. reciprocating spiral mixing machine 2, is the reciprocating spiral mixing machine with heating and heat insulation function purchased in market.It is main It is stirring, mix asphalt and SBS and additive to want function, while making the temperature automatic control of material at 130 DEG C -180 DEG C.Peace Dress inclines 2 degree as shown in Figure 1.
3. single-stage high-shear emulsion machine 4, is single-stage high-shear emulsion machine purchased in market(Or pre- cutter), major function be by Material is further mixed, disperseed, sheared by technological requirement.
4. combined static blender 6, is the single tube static mixer with heating and heat insulation function purchased in market, according to life The design requirement of production capacity power, is made the component of multitube parallel.Major function be material is sufficiently stirred for, is mixed, it is swelling.
5. multi-stage high shear mulser 7, buys from market, and major function is by the material from combined static blender Repeatedly sheared, material is reached the fineness of technological requirement and complete swelling.
The road asphalt that the present invention is used is, marked as 70# or 90# road asphalts, can be selected according to specific requirement.
SBS used is linear, and styrene and butadiene block compare 30/70, molecular weight 10-20 ten thousand.
Additive used is aromatic naphtha, 100 DEG C of kinematic viscosity 10-35mm2/S.40 DEG C of kinematic viscosity 40-50mm of machine oil ²/S。
Microwax, stearic acid used, 65 DEG C -120 DEG C of softening point.
The conduction oil or electric heating automatic control system that the control of operation temperature can be configured by relevant connection pipeline are realized.
Embodiment 1:
The device and method of the full-closed zero discharge continuous prodution modified pitch that the present invention is provided, prepares SBS modified pitch Technological process as shown in Figure 1:First by conduction oil or electric heating automatic control system, set all according to operation index The temperature of equipment and connecting pipe, after temperature touches the mark, the matrix pitch from storage tank, 120 DEG C -150 DEG C of temperature, by pitch The input reciprocating spiral of pump 1 mixing machine 3, meanwhile, the SBS and additive agent mixture material being pre-mixed in proportion(Wherein by weight Gauge:SBS4 parts, 3 parts of aromatic naphtha, 3 parts of microwax), reciprocating spiral mixing machine 3 is added by forced feed machine 2.Regulation drip The motor speed of blue or green pump 1 and forced feed machine 2, makes matrix pitch(By weight)Reach 90 parts(The SBS of matrix pitch 90 with add Plus agent composition material 10).
Since reciprocating spiral mixing machine 3, later equipment and the temperature of connecting pipe are promoted to 160 DEG C -180 DEG C, After SBS mixes in reciprocating spiral mixing machine 3 with additive agent mixture material with matrix pitch, the continuous uninterrupted single-stage that enters is cut Cut machine 4 tentatively dispersion, shearing, then stir by the input of bitumenpump 5 combined static blender 6, mix, it is swelling after, into many Level high-shear emulsion machine 7, is finally input into storage tank or bitumen concrete mixing station by bitumenpump 8.Input storage tank or bitumen concrete mixing station Modified pitch temperature is not less than 175 DEG C, reaches the index request of relevant national standard.Reciprocating spiral mixing machine 3, single-stage is high to be cut Cut mulser 4, bitumenpump 5, multi-stage high shear mulser 7, bitumenpump 8 motor power (output) it is reasonable according to specific production capacity Distribute rationally, running at full capacity after startup.
Embodiment 2:
The device and method of the full-closed zero discharge continuous prodution modified pitch that the present invention is provided, prepares SBS modified pitch Technological process as shown in Figure 1:First by conduction oil or electric heating automatic control system, set all according to operation index The temperature of equipment and connecting pipe, after temperature touches the mark, the matrix pitch from storage tank, 110 DEG C -130 DEG C of temperature, by pitch The input reciprocating spiral of pump 1 mixing machine 3, meanwhile, the SBS and additive agent mixture material being pre-mixed in proportion(Wherein by weight Gauge:4 parts of SBS4 parts, 6 parts of machine oil, 4 parts of microwax or stearic acid), reciprocating spiral mixing machine is added by forced feed machine 2 3.The motor speed of regulation bitumenpump 1 and forced feed machine 2, makes matrix pitch(By weight)Reach 86 parts(Matrix pitch 86 SBS and additive agent mixture material 14).
Since reciprocating spiral mixing machine 3, later equipment and the temperature of connecting pipe are promoted to 130 DEG C -150 DEG C, After SBS mixes in reciprocating spiral mixing machine 3 with additive agent mixture material with matrix pitch, the continuous uninterrupted single-stage that enters is cut Cut machine 4 tentatively dispersion, shearing, then stir by the input of bitumenpump 5 combined static blender 6, mix, it is swelling after, into many Level high-shear emulsion machine 7, is finally input into storage tank or bitumen concrete mixing station by bitumenpump 8.Input storage tank or bitumen concrete mixing station Modified pitch temperature is not higher than 150 DEG C, reaches the index request of relevant national standard.Reciprocating spiral mixing machine 3, single-stage is high to be cut Mulser 4, bitumenpump 5, multi-stage high shear mulser 7, the motor power (output) of bitumenpump 8 is cut to be matched somebody with somebody according to specific production capacity Put, running at full capacity.
The embodiment of the present invention, at 130 DEG C -150 DEG C, the modified pitch temperature of production is not higher than production technology temperature control It is 150 DEG C, not only energy-saving, also substantially reduce disposal of pollutants.
To ensure production safety, automatic control system installs three sets of interlocks to process units of the present invention:1. all devices With the setting that the temperature of connecting pipe is not up to operation index, any equipment cannot all start.2. drip is first started after temperature is up to standard Blue or green pump(8), work well and restart multi-stage high shear mulser(7), bitumenpump is started successively(5), single-stage high-shear emulsion machine (4), reciprocating spiral mixing machine(3), after all working well, bitumenpump could be started(1)With forced feed machine(2).3. give birth to When producing operation,(3)-(8)In any equipment shut down suddenly, bitumenpump(1)With forced feed machine(2)Will be tight Suddenly shut down.
The present invention changes traditional SBS Production Process of Modified Bitumen, qualified to output from the matrix pitch from storage tank SBS modified pitch, the totally-enclosed serialization of production process, does not have any waste gas discharge;Process route is concise, simple to operate, takes up an area Area is small, very convenient supporting with bitumen concrete mixing station, can accomplish that startup-shutdown is produced, it is necessary to many simultaneously with bitumen concrete mixing station Few SBS modified pitch just produce how much, reduce the multiple transport of pitch and modified pitch and heat repeatedly to modified pitch matter The influence of amount, at the same it is energy-saving, it is cost-effective.
The device and method of full-closed zero discharge continuous prodution modified pitch of the invention, can also by being formulated design Production high-viscosity modified asphalt, rubber powder modified asphalt, color asphalt and warm-mixed asphalt.
The device and method of full-closed zero discharge continuous prodution modified pitch of the invention, is not limited to above-described embodiment.

Claims (4)

1. a kind of device of full-closed zero discharge continuous prodution modified pitch, it is characterised in that by three bitumenpumps, one it is strong Feeding machine processed, a reciprocating spiral mixing machine, single-stage high-shear emulsion machine, combined static blender, one Multi-stage high shear mulser, and the pipeline composition of above equipment is connected according to technological requirement;Wherein, bitumenpump(1), force feed Material machine(2)Reciprocating spiral mixing machine is connected respectively(3), reciprocating spiral mixing machine(3)Connection single-stage high-shear emulsion machine(4) Afterwards, it is sequentially connected bitumenpump(5), combined static blender(6), multi-stage high shear mulser(7), bitumenpump(8);Bitumenpump (8)Outlet by pipeline connect modified pitch storage tank or bitumen concrete mixing station.
2. it is a kind of based on claim 1 described device produce modified pitch method, it is characterised in that idiographic flow is as follows:Come From 120 DEG C -150 DEG C of the matrix pitch temperature of storage tank, by bitumenpump(1)Pump is input into reciprocating spiral mixing machine(3), meanwhile, The SBS and the compound of additive being pre-mixed in proportion, by forced feed machine(2)Add reciprocating spiral mixing machine (3);The mixed material of SBS and additive, in reciprocating spiral mixing machine(3)It is interior mix with matrix pitch after, it is continuous uninterrupted Into single-stage high-shear emulsion machine(4)In, preliminary dispersion, shearing, then by bitumenpump(5)It is input to combined static blender (6)Be stirred, mix, it is swelling, subsequently into multi-stage high shear mulser(7), finally by bitumenpump(8)Input storage tank or drip Qing Tong mixing stations.
3. the method for production modified pitch according to claim 2, it is characterised in that the SBS and additive formulations Composition, by weight:
Matrix pitch 80-90 parts;
SBS 2-7 parts;
Additive:Aromatic naphtha or machine oil 4-10 parts;
Additive:Microwax and/or stearic acid 3-10 parts.
4. it is according to claim 3 production modified pitch method, it is characterised in that in production process, if additive It is aromatic naphtha and microwax, operation temperature is controlled at 160 DEG C -180 DEG C in addition to forced feed machine;If additive is machine oil With microwax and stearic acid, then in addition to forced feed machine, control is at 130 DEG C -150 DEG C for operation temperature.
CN201710143294.7A 2017-03-11 2017-03-11 A kind of full-closed zero discharge continuous production modified pitch device and method Active CN106861544B (en)

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Cited By (6)

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CN109825323A (en) * 2019-04-03 2019-05-31 杭州欣亿广告有限公司 A kind of equipment of producing modified asphalt
CN110201621A (en) * 2019-07-04 2019-09-06 河北交科材料科技有限公司 A kind of tubular type modified pitch batch mixer
CN110639413A (en) * 2019-09-10 2020-01-03 北京丰泽华夏生态环境科技有限公司 Mixing and melting device for preparing modified emulsified asphalt and using method
CN110684366A (en) * 2019-10-23 2020-01-14 李振华 Preparation method of multi-variety full-granular modified asphalt for asphalt refinery
CN111632549A (en) * 2020-06-30 2020-09-08 安徽锐达橡胶科技有限公司 Continuous automatic production system and method applied to modified asphalt
RU2763721C1 (en) * 2020-12-30 2021-12-30 Общество с ограниченной ответственностью "ПРОГРАММА" Method and unit for continuous production of a polymer bitumen binder in-line

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CN111632549A (en) * 2020-06-30 2020-09-08 安徽锐达橡胶科技有限公司 Continuous automatic production system and method applied to modified asphalt
RU2763721C1 (en) * 2020-12-30 2021-12-30 Общество с ограниченной ответственностью "ПРОГРАММА" Method and unit for continuous production of a polymer bitumen binder in-line

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