CN202705321U - Biomass pyrolysis vinegar cooling and collecting device - Google Patents

Biomass pyrolysis vinegar cooling and collecting device Download PDF

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Publication number
CN202705321U
CN202705321U CN 201220251099 CN201220251099U CN202705321U CN 202705321 U CN202705321 U CN 202705321U CN 201220251099 CN201220251099 CN 201220251099 CN 201220251099 U CN201220251099 U CN 201220251099U CN 202705321 U CN202705321 U CN 202705321U
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CN
China
Prior art keywords
vinegar
cooling
collecting device
funnel
biomass pyrolysis
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Expired - Fee Related
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CN 201220251099
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Chinese (zh)
Inventor
时新宁
李健
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Senmiao Technology Group Ltd By Share Ltd
Original Assignee
NINGXIA FORESTRY INSTITUTE Co Ltd
NINGXIA SENMIAO SEED INDUSTRY BIOLOGICAL ENGINEERING Co Ltd
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Priority to CN 201220251099 priority Critical patent/CN202705321U/en
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Abstract

The utility model relates to biomass pyrolysis gasification devices, in particular to a biomass pyrolysis vinegar cooling and collecting device which comprises vinegar separating condensers. The biomass pyrolysis vinegar cooling and collecting device is characterized in that funnel-shaped flow collectors (7) are mounted at bottoms of the vinegar separating condensers, a vinegar collector (8) is connected to an outlet of each funnel-shaped flow collector (7), and a vinegar outlet (9) is arranged on each vinegar collector (8). An existing vinegar collecting device (see also from the first patent of the background technology) is modified, water is still used as sealing liquid at the bottoms of the condensers, but is no longer used for collecting cold vinegar and is only used for preventing explosion, accordingly, the shortcoming of low concentration of vinegar produced when original vinegar production equipment just starts to produce the vinegar is overcome, the biomass pyrolysis vinegar cooling and collecting device has the advantages of simple structure, capability of preventing explosion, good sealing performance, convenience in maintenance and the like, the density (in the unit of g/cm<3>) of reed vinegar is increased to 1.005 from the original 1.001 when reed vinegar production is just started, the density of the produced vinegar is stable, and application to follow-up agricultural production is facilitated.

Description

The liquid cooling of a kind of biomass pyrolytic vinegar is collection device but
Technical field
The utility model relates to the biomass pyrogenation gasification device, and the liquid cooling of especially a kind of biomass pyrolytic vinegar is collection device but.
Background technology
Patent one, gas-liquid separation purification system (the patent No.: 200910032957.3 that is used for the agriculture and forestry biomass materials pyrolysis gas, publication number CN101564630), its apparatus structure is the entrance of gas inlet pipe access cyclonic separator, the outlet needle tube type of cyclonic separator and the entrance of condenser join, the entrance of the outlet access spray equipment of needle tube type condenser, the entrance of the outlet access static decoking device of spray equipment, the outlet access gas-holder of static decoking device, the outlet of gas-holder connects cleaning combustible gas output tube.The advantage of its device is scientific structure, reasonable, adopt the needle tube type condenser to substitute coil tube type or return pipe formula condenser, not only use, easy to maintenance, and use native system and the gas that biomass pyrolytic produces fully can be separated, purifies, reach the requirement of oil engine combustion gas and air feed, form continuously continual stable air feed.
Patent two, wood vinegar tar cooling-collecting device (the patent No.: 201020275662.7, publication number CN201729815U), its device comprises gas feed, pneumatic outlet, heat exchanger shell, entrance of cooling water, cooling water outlet, heat transfer tube, fin, interchanger bottom collection bucket, interchanger bottom leakage fluid dram, shell separator, baffle, separator base plate, separator bottom collection bucket, separator bottom leakage fluid dram, separator gas import, separator gas outlet, interchanger base plate.Feature is that interchanger and separator are all vertically installed, and links to each other by straight tube.Pyrolysis gas is cooled through heat exchange after entering interchanger, and a small amount of wood vinegar and tar liquid collect in base plate in interchanger, and inflow heat exchanger bottom collection bucket, and most of tar and wood vinegar enter in the separator with pyrolysis gas.Pyrolysis gas is carried the baffle in tar and the continuous impingement separators of wood vinegar secretly, and in knockout process, separate, pyrolysis gas after the separation is discharged from the separator gas outlet, and tar and wood vinegar under separating stay along baffle plate, and flows into separator bottom collection bucket.The utility model has realized containing cooling and the liquid collecting of tar and wood vinegar high temperature pyrolysis gas, have simple in structure, good airproof performance, the advantage such as easy to maintenance and reusable.
In addition, patent three, the coke tar vinegar liquid condensing separating device of the Biomass Gasification ﹠ Power Generation (patent No.: 200720124862.0, publication number CN201071359), its apparatus structure is Stainless Steel Wire screen plate on the device of middle and upper part in the case shell of coke tar vinegar liquid condensing separator, Stainless Steel Wire screen plate under the device of middle and lower part, there is condensate pipe the centre, water inlet pipe and the rising pipe of condensate pipe two ends welding passband valve, shell wall welds respectively pass-out tracheae B one end and escape pipe C one end between the top shell of upper Stainless Steel Wire screen plate and case shell, and the other end of escape pipe C inserts in the gas-holder tank.Have simple and compact for structurely, fabrication and installation are convenient, are conducive to condensation separation, reclaim useful matter, reduce the characteristics such as environmental pollution.
The most obvious defective of above prior art is: the utility model wood vinegar tar cooling-collecting device of the rich bioenergy Science and Technology Ltd. of the coke tar vinegar liquid condensing separating device of the utility model Biomass Gasification ﹠ Power Generation of Li Xiaokun and Hefei moral invention lacks safe explosion-proof device, pyrolysis might produce back draft in producing, and the gas-liquid separation purification system that is used for the agriculture and forestry biomass materials pyrolysis gas of Nanjing Forestry University's invention is provided with explosion-proof equipment, its explosion-proof equipment is to adopt hydraulic seal in vinegar liquid cooling condenser bottom, although avoided explosion hazard, but the vinegar liquid that condensation is collected is to flow out from the bottom after mixing with sealed bottom liquid (water), a kind of new raw material vinegar liquid of each production need to be changed the sealing fluid water, and the sealing water yield is very large, it is very low to begin concentration to the vinegar liquid that makes each new raw material production, needing to produce large content of starting materials and expending just can reach for a long time needs concentration, and can not production short run vinegar liquid product.
The utility model content
The purpose of this utility model provides but collection device of a kind of simple in structure, explosion-proof, good airproof performance and biomass pyrolytic vinegar liquid cooling easy to maintenance.
The liquid cooling of a kind of biomass pyrolytic vinegar is collection device but, comprise vinegar liquid separation condenser, be characterized in: in described vinegar liquid separation condenser bottom the funnel-form current collector is installed, the outlet of this funnel-form current collector connects a vinegar collection, is provided with vinegar liquid leakage fluid dram at this vinegar collection.
Wherein vinegar liquid separation condenser has two, is separately installed with a funnel-form current collector in each vinegar liquid separation condenser bottom, and passes through pipeline connection between two funnel-form current collectors.
The utility model improves existing vinegar liquor collecting device (referring to the patent one of background technology), increase a funnel-form current collector and a small-sized vinegar collection in original vinegar liquid separation condenser bottom, directly collect the vinegar liquid of condensation, the vinegar liquid sealing that the explosion-proof use self of small-sized vinegar collection produces; Condensation sealed bottom liquid still makes water, but do not regather cold vinegar liquid, only do explosion-proof use, overcome so vinegar liquid concentration that former vinegar liquid production unit begins to produce low and shortcoming, have simple in structure, explosion-proof, good airproof performance, the advantage such as easy to maintenance is produced the liquid-tight degree (g/cm of reed vinegar of beginning 3) bring up to 1.005 by original 1.001, and the liquid-tight degree of vinegar of producing is stable, is convenient to the application in the follow-up agriculture production.
Description of drawings
Accompanying drawing 1 is structural representation of the present utility model.
Among the figure 1 is gas feed, the 2nd, pneumatic outlet, the 3rd, condenser shell, the 4th, entrance of cooling water, the 5th, cooling water outlet, the 6th, heat transfer tube, the 7th, funnel-form current collector, the 8th, vinegar collection, the 9th, vinegar liquid leakage fluid dram, the 10th, suspension chain, the 11st, explosive-proof sealed pond.
Embodiment
As shown in Figure 1, the liquid cooling of a kind of biomass pyrolytic vinegar is collection device but, comprises vinegar liquid separation condenser, in described vinegar liquid separation condenser bottom funnel-form current collector 7 is installed, the outlet of this funnel-form current collector 7 connects a vinegar collection 8, is provided with leakage fluid dram at this vinegar collection 8.Wherein vinegar liquid separation condenser has two, is separately installed with a funnel-form current collector 7 in each vinegar liquid separation condenser bottom, and passes through pipeline connection between two funnel-form current collectors 7.
Biomass pyrolytic vinegar of the present utility model liquid cooling but collection device structure as shown in Figure 1, mainly comprise but collection device of vinegar liquid cooling that gas feed 1, pneumatic outlet 2, condenser shell 3, entrance of cooling water 4, cooling water outlet 5, heat transfer tube 6, funnel-form current collector 7, vinegar collection 8, vinegar liquid leakage fluid dram 9, suspension chain 10, explosive-proof sealed pond 11 form.Two cover vinegar liquid separation condenser series connection are vertically installed.
High temperature pyrolysis gas has gas feed 1 to enter condenser, and through heat transfer tube 6, again by pneumatic outlet 2 eductor condensers.Gas through in the process of heat transfer tube 6 with pipe outside water coolant carry out heat exchange, gas is cooled, the a large amount of vinegar liquid that wherein contain and a small amount of tar become liquid state in cooling, flow to funnel-form current collector 7 along heat transfer tube 6 inwalls, the vinegar liquid of collection is being introduced vinegar collection 8 from 9 discharges of vinegar liquid leakage fluid dram by pipeline.

Claims (2)

1. but collection device of biomass pyrolytic vinegar liquid cooling, comprise vinegar liquid separation condenser, it is characterized in that: in described vinegar liquid separation condenser bottom funnel-form current collector (7) is installed, the outlet of this funnel-form current collector (7) connects a vinegar collection (8), is provided with vinegar liquid leakage fluid dram (9) at this vinegar collection (8).
2. but collection device of a kind of biomass pyrolytic vinegar as claimed in claim 1 liquid cooling, it is characterized in that: wherein vinegar liquid separation condenser has two, be separately installed with a funnel-form current collector (7) in each vinegar liquid separation condenser bottom, and pass through pipeline connection between two funnel-form current collectors (7).
CN 201220251099 2012-05-31 2012-05-31 Biomass pyrolysis vinegar cooling and collecting device Expired - Fee Related CN202705321U (en)

Priority Applications (1)

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CN 201220251099 CN202705321U (en) 2012-05-31 2012-05-31 Biomass pyrolysis vinegar cooling and collecting device

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CN 201220251099 CN202705321U (en) 2012-05-31 2012-05-31 Biomass pyrolysis vinegar cooling and collecting device

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105219447A (en) * 2015-09-24 2016-01-06 湖南省金本低碳科技有限公司 The separating of oil purification-recovery system of a kind of biomass gas-liquid
CN105300136A (en) * 2015-11-23 2016-02-03 吉林省汇能能源股份有限公司 Biomass gas heat exchange device
CN105368496A (en) * 2015-11-30 2016-03-02 南京林业大学 Process method for cogenerating electricity, charcoal, heat and fertilizer through gasified gas supply of biomass
TWI704009B (en) * 2019-10-22 2020-09-11 行政院原子能委員會核能研究所 Oil-gas separation system and its use

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105219447A (en) * 2015-09-24 2016-01-06 湖南省金本低碳科技有限公司 The separating of oil purification-recovery system of a kind of biomass gas-liquid
CN105219447B (en) * 2015-09-24 2017-08-29 湖南湘益低碳新能源有限责任公司 A kind of biomass gas-liquid oil separation purification-recovery system
CN105300136A (en) * 2015-11-23 2016-02-03 吉林省汇能能源股份有限公司 Biomass gas heat exchange device
CN105368496A (en) * 2015-11-30 2016-03-02 南京林业大学 Process method for cogenerating electricity, charcoal, heat and fertilizer through gasified gas supply of biomass
CN105368496B (en) * 2015-11-30 2018-04-03 南京林业大学 A kind of biomass gasification and gas-supply coproduction electricity, charcoal, heat, the process of fertilizer
TWI704009B (en) * 2019-10-22 2020-09-11 行政院原子能委員會核能研究所 Oil-gas separation system and its use

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee
CP01 Change in the name or title of a patent holder

Address after: Victory Street Xingqing District of Yinchuan City No. 1059 the Ningxia Hui Autonomous Region 750004

Patentee after: Ningxia Senmiao Technology Group Limited by Share Ltd

Patentee after: Ningxia Forestry Institute Co., Ltd.

Address before: Victory Street Xingqing District of Yinchuan City No. 1059 the Ningxia Hui Autonomous Region 750004

Patentee before: Ningxia Senmiao Seed Industry Biological Engineering Co., Ltd.

Patentee before: Ningxia Forestry Institute Co., Ltd.

CP01 Change in the name or title of a patent holder

Address after: Victory Street Xingqing District of Yinchuan City No. 1059 the Ningxia Hui Autonomous Region 750004

Co-patentee after: Ningxia Forestry Institute Co., Ltd.

Patentee after: Senmiao Technology Group Limited by Share Ltd

Address before: Victory Street Xingqing District of Yinchuan City No. 1059 the Ningxia Hui Autonomous Region 750004

Co-patentee before: Ningxia Forestry Institute Co., Ltd.

Patentee before: Ningxia Senmiao Technology Group Limited by Share Ltd

CP01 Change in the name or title of a patent holder
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130130

Termination date: 20210531

CF01 Termination of patent right due to non-payment of annual fee