CN103411128A - Integrated storage tank supercharge and gasification sledge - Google Patents
Integrated storage tank supercharge and gasification sledge Download PDFInfo
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- CN103411128A CN103411128A CN2013100918339A CN201310091833A CN103411128A CN 103411128 A CN103411128 A CN 103411128A CN 2013100918339 A CN2013100918339 A CN 2013100918339A CN 201310091833 A CN201310091833 A CN 201310091833A CN 103411128 A CN103411128 A CN 103411128A
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Abstract
The invention discloses an integrated storage tank supercharge and gasification sledge which comprises a horizontal storage tank, wherein the horizontal storage tank has a bilayer structure and is used for storing a low-temperature medium, a vaporizer is arranged at the back end of the horizontal storage tank and is used for vaporizing the low-temperature medium in the horizontal storage tank so as to facilitate air feed, a top self-supercharger and a bottom self-supercharger which are used for supercharging the horizontal storage tank from top and bottom sides are respectively arranged below two wings of the horizontal storage tank, an operation valve system is arranged at the front end of the horizontal storage tank and at least comprises an unloading process, a supercharge process and a safe scattering process of the horizontal storage tank and a vaporization air feed process of the vaporizer, the horizontal storage tank, the vaporizer, the top self-supercharger, the bottom self-supercharger and operation valve system are fixedly arranged in a frame with the appearance meeting a standard container size so as to form a storage tank supercharge and gasification sledge with an storage, supercharge and gasification integration structure. The integrated storage tank supercharge and gasification sledge disclosed by the invention has the characteristics of high integration level, small floor space, sensitive movement, simplicity in installation and fastness in operation.
Description
Technical field
The present invention relates to a kind of gasification storage tank device, specifically a kind of integrated storage tank supercharging gasification sledge.
Background technique
In recent years, along with the fast-developing of China's economy and to the demand of environmental protection and energy saving, the every profession and trade of national economy is increasing for the demand of inflammable gas.And in prior art, traditional blowing model is mostly the equipment such as storage tank, vaporizer, adjusting pressure device separately and separate one-tenth piece between its each equipment is installed in scene.The method of construction and installation is carried out at this scene, and not only long construction period, and floor space is wide and relatively high to basis and field requirement, therefore is unfavorable for the lifting of enterprises production efficiency and the reduction of cost of production.If moreover because enterprise need to plan again, its relevant air feed equipment just must re-start layout, equipment Foundations therebetween, integral layout and construction etc. also will be readjusted, and so not only waste time and energy, and also are unfavorable for resuming production fast of enterprise.Therefore, traditional blowing model falls behind, and is difficult to meet the needs of Economic Development.
Summary of the invention
Technical problem to be solved by this invention is for above-mentioned prior art present situation, integrates storage, supercharging, gasification and low to on-the-spot installation environment requirement and provide, a kind of integrated storage tank supercharging gasification sledge that floor space is little, easy and simple to handle, safe.
The present invention solves the problems of the technologies described above the technological scheme adopted: a kind of integrated storage tank supercharging gasification sledge, comprise that double layer construction is be used to storing the horizontal tank tank of cryogenic media, the rear end of horizontal tank tank is provided with the vaporizer of cryogenic media vaporization in the horizontal tank tank being convenient to air feed, the both wings below of this horizontal tank tank is respectively arranged with carries out upper automatic pressure intensifier and the lower automatic pressure intensifier of supercharging to the horizontal tank tank from upper and lower two sides, the front end of horizontal tank tank is provided with the operated valve system, the operated valve system comprises the flow process of unloading of horizontal tank tank at least, the vaporization air feed flow process that supercharging flow process and safety are diffused flow process and vaporizer, horizontal tank tank, vaporizer, upper automatic pressure intensifier, lower automatic pressure intensifier and operated valve system are fixedly mounted on profile and meet in the framework of standardised container size and form a kind of storage tank supercharging type gasification sledge that storage, supercharging, gasification are structure as a whole that collects.
For optimizing technique scheme, the measure of taking also comprises:
Above-mentioned horizontal tank tank is comprised of inner container and the outer field groove ladle bowl of internal layer, between groove ladle bowl and inner container, be provided with vacuum heat-insulating layer, in this vacuum heat-insulating layer, be filled with pearlife, the rear portion of groove ladle bowl is shaped with the urceolus venting, the anti-blasting device of shell is installed on this urceolus venting, and on the groove ladle bowl, have vacuum orifice and survey vacuum port, described vacuum orifice and survey vacuum port are separately installed with vacuum pumping valve and survey vacuum valve.
Above-mentioned vaporizer is that air is heated and carried out the air temperature type vaporizer of cold and hot exchange, the heat exchanging fin tube that this air temperature type vaporizer is combined side by side by a plurality of vertical installations forms, between two adjacent heat exchanging fin tubes, leave the gap of circulation of air, heat exchanging fin tube is connected and is communicated successively by bridge piece.
The above-mentioned flow process of unloading is included as the interface that fills of horizontal tank tank inner container topping up, this fills interface and through top liquid inlet pipe and bottom liquid inlet pipe, is connected with top feed liquor interface and bottom liquid entering hole that the horizontal tank tank is shaped with respectively, top feed liquor operating valve is installed on the liquid inlet pipe of top, bottom feed liquor operating valve is installed on the liquid inlet pipe of bottom.
Above-mentioned supercharging flow process comprises that the upper pressure inlet of the upper automatic pressure intensifier of an end connection is connected the lower pressure inlet of lower automatic pressure intensifier with an end, and supercharging gas phase operation valve is installed in the pipeline of upper pressure inlet, boost pressure regulation operating valve and supercharging liquid phase operating valve are installed in the pipeline of lower pressure inlet successively, the other end of upper pressure inlet is connected with the upper supercharging interface of the connection horizontal tank tank inner container that the horizontal tank tank is shaped with, the other end of lower pressure inlet is connected with horizontal tank tank bottom liquid entering hole, and is connected with pressure-equalizing pipe between upper automatic pressure intensifier and lower automatic pressure intensifier.
Above-mentioned vaporization air feed flow process comprises liquid outlet and the liquid transport pipeline between air temperature type vaporizer vaporization import and the supply air line that is arranged on air temperature type vaporizer air feed port be communicated with the horizontal tank tank is shaped with, on liquid transport pipeline, between air temperature type vaporizer vaporization import, liquid output function valve and emergency cut-off operating valve are installed successively by horizontal tank tank liquid outlet, gas output function valve is installed on supply air line.
Above-mentioned safety is diffused flow process and is comprised the bulk storage pipeline that is provided with concentrated bulk storage mouth, on this bulk storage pipeline and horizontal tank tank, set up respectively between the supercharging interface inner core safety anti-explosive pipe-line system and manual blowdown piping are arranged, manually in blowdown piping, manual emptying manipulation valve is installed, inner core safety anti-explosive pipe-line system comprises the first explosion-proof pipeline and the second explosion-proof pipeline of installing side by side through three-way switch valve, the first inner core rupture disk and the first inner core safety valve are installed in the first explosion-proof pipeline, the second inner core rupture disk and the second inner core safety valve are installed in the second explosion-proof pipeline.
One end of above-mentioned bulk storage pipeline is arranged on blowdown valve, before on supply air line, being positioned at gas output function valve, setting up air feed raffinate loop and the air feed safety dumping loop all communicated with the bulk storage pipeline arranged respectively, air feed residual liquid discharge valve is installed on air feed raffinate loop, the air feed safety dumping is equipped with the steam line safety valve on loop, before on liquid transport pipeline, being positioned at the emergency cut-off operating valve and after liquid output function valve, setting up the pressure regulation pipeline that is communicated with supercharging interface on the horizontal tank tank is arranged, reduction regulation operating valve and economic open valve are installed on this pressure regulation pipeline successively.
Above-mentioned horizontal tank tank has gas phase interface and liquid phase interface, the gas phase interface is equipped with the gas phase pipe, the liquid phase interface is equipped with liquid-phase tube, gas phase pipe and liquid-phase tube are connected through the level meter equilibrium valve, and the level meter gas valve is installed in the gas phase pipe, the level meter liquid phase valve is installed in liquid-phase tube, the gas phase connecting end of level meter equilibrium valve and liquid phase connecting end are drawn respectively pressure gauge and level meter are installed, the horizontal tank tank is fitted with relief valve, and fill jointing be equipped with the bulk storage pipeline, communicate fill the residual liquid discharge valve.
Above-mentioned framework is long cube structure, and the bight of framework all adopts the container-type corner fittings to connect, the horizontal tank tank is in fixed saddle is fixed in framework, the front end of framework is equipped with the operating valve protective door, this operating valve protective door is two-door laterally opened, the horizontal tank tank survey full packages is installed, the supercharging safety line communicated with the bulk storage pipeline is installed on upper pressure inlet between supercharging gas phase operation valve and automatic pressure intensifier, on this supercharging safety line, be fitted with the pressure pipeline safety valve.
Compared with prior art, the present invention mainly contains following advantage:
1, level of integration is high: the present invention all is arranged in horizontal tank tank, automatic pressure intensifier, vaporizer, operated valve system, operating valve protective door in one standard container framework, and framework is the standard container size, skid-mounted device is compact structure not only, space availability ratio is high, and attractive in appearance, the lifting of being more convenient for, transportation and storage.
2, floor space is little: due to the high integration of this skid-mounted device, all storages, supercharging, vaporization and relevant operation system all are arranged in framework, its area occupied less, and the placement that is beneficial to equipment is installed.
3, swift to operate: as because the operated valve in whole equipment all is arranged in an end in framework, therefore, during operation, only need to carry out associative operation to a place and get final product, without the frequent changes place, carry out the operation of valve, can save the operating time, and operation rapidly.
4, mobile sensitive: because relevant this equipment all is integrated in a standard container framework, and four jiaos of frameworks adopt the container-type corner fittings, therefore, in the middle of transportation and handling process, suitable quick and safe, and lifting cost but can, without frequent lifting.
5, install simply: because the bottom distribution area of this equipment is wide, over all Integration, for its installation requirement, relatively simple, only need look for a smooth cement court, without carrying out storage tank basis and the processing of relevant device basis, can greatly reduce mounting cost, simultaneously, also quick for installation.
The accompanying drawing explanation
Fig. 1 is the structural representation of the embodiment of the present invention;
Fig. 2 is the plan structure figure of Fig. 1;
Fig. 3 is the not right TV structure figure during fitting operation valve protective door of Fig. 1;
Fig. 4 is the left TV structure figure of Fig. 1;
Fig. 5 is the structural drawing after Fig. 3 fitting operation valve protective door;
Fig. 6 is schematic flow sheet of the present invention.
Embodiment
Below in conjunction with accompanying drawing, embodiments of the invention are described in further detail.
Fig. 1 is to Figure 6 shows that structural representation of the present invention.
Reference character wherein is: vacuum pumping valve A1, survey vacuum valve A2, pressure gauge P, level meter L, horizontal tank tank 1, vacuum heat-insulating layer 1a, top feed liquor interface 1b, bottom liquid entering hole 1c, inner container 11, groove ladle bowl 12, urceolus venting 12a, vacuum orifice 121, survey vacuum port 122, pearlife 13, vaporizer 2, air temperature type vaporizer 21, heat exchanging fin tube 22, bridge piece 23, upper automatic pressure intensifier 31, lower automatic pressure intensifier 32, pressure-equalizing pipe 33, operated valve system 4, top feed liquor operating valve 41a, bottom feed liquor operating valve 41b, fill residual liquid discharge valve 41c, fill interface 411, top liquid inlet pipe 412, bottom liquid inlet pipe 413, supercharging gas phase operation valve 42a, boost pressure regulation operating valve 42b, supercharging liquid phase operating valve 42c, pressure pipeline safety valve 42d, upper pressure inlet 421, lower pressure inlet 422, liquid output function valve 43a, emergency cut-off operating valve 43b, gas output function valve 43c, air feed residual liquid discharge valve 43d, steam line safety valve 43e, reduction regulation operating valve 43f, economic open valve 43g, liquid transport pipeline 431, supply air line 432, bulk storage pipeline 44, manual emptying manipulation valve 44a, the first inner core rupture disk 44b, the first inner core safety valve 44c, the second inner core rupture disk 44d, the second inner core safety valve 44e, three-way switch valve 44f, blowdown valve 44g, concentrate bulk storage mouth 441, level meter equilibrium valve 45a, level meter gas valve 45b, level meter liquid phase valve 45c, gas phase pipe 451, liquid-phase tube 452, shell is prevented blasting device 5, relief valve 6, survey full packages 7, fixed saddle 8, framework 9, operating valve protective door 91.
As shown in Figures 1 to 6, a kind of integrated storage tank supercharging gasification sledge of the present invention, comprise that double layer construction is be used to storing the horizontal tank tank 1 of cryogenic media, the rear end of horizontal tank tank 1 is provided with is convenient to the vaporizer 2 for the rear end equipment air feed by the interior cryogenic media vaporization of horizontal tank tank 1, the both wings below of this horizontal tank tank 1 is respectively arranged with carries out upper automatic pressure intensifier 31 and the lower automatic pressure intensifier 32 of upper and lower supercharging to horizontal tank tank 1 from upper and lower two sides, the front end of horizontal tank tank 1 is provided with operated valve system 4, this operated valve system 4 comprises the flow process of unloading of horizontal tank tank at least, the vaporization air feed flow process that supercharging flow process and safety are diffused flow process and vaporizer, horizontal tank tank 1, vaporizer 2, upper automatic pressure intensifier 31, lower automatic pressure intensifier 32 and operated valve system 4 are fixedly mounted on a profile and meet that the interior formation of framework 9 of standardised container size is a kind of collects the storage tank supercharging type gasification sledge that storage, supercharging, gasification are structure as a whole.The present invention concentrates storage, supercharging, vaporization and operation system to be fitted in standard container framework 9 inside, changed the unloading of traditional blowing model, supercharging, gasification, safety and the scattered distribution pattern of system such as diffused, integral device quick construction not only, low to basis and field requirement, and simple and efficient to handle, safety properties is high.Framework 9 boundary dimension meet the standardised container size, are convenient to the use of integrated moving carrying.Operated valve system 4 concentrates on the front end of framework 9, and convenient operation is controlled, and can operate without frequently walking about.The present invention has that level of integration is high, floor space is little, mobile sensitive and characteristics simple and swift to operate are installed.
For further optimizing the structure of this sledge, in embodiment, as shown in Figure 6, horizontal tank tank 1 is comprised of inner container 11 and the outer field groove ladle bowl 12 of internal layer, 11 of groove ladle bowl 12 and inner containers are provided with vacuum heat-insulating layer 1a, in this vacuum heat-insulating layer 1a, be filled with pearlife 13, groove ladle bowl 12 of the present invention is shaped with the pearlife feeding port, can fill by the pearlife feeding port, as can see from Figure 1, the rear portion of groove ladle bowl 12 is shaped with urceolus venting 12a, the anti-blasting device 5 of shell is installed on this urceolus venting 12a, and on groove ladle bowl 12, have vacuum orifice 121 and survey vacuum port 122, vacuum orifice 121 and survey vacuum port 122 are separately installed with vacuum pumping valve A1 and survey vacuum valve A2.The main use of storing cryogenic media that rises of horizontal tank tank of the present invention 1, the Sandwich filling pearlife 13 that groove ladle bowl 12 and inner container are 11 vacuumize can better be until insulation effect.
In embodiment, as shown in Figure 1, Figure 2 and Figure 4, the air temperature type vaporizer 21 that vaporizer 2 is heated and carried out cold and hot exchange for air, the heat exchanging fin tube 22 that this air temperature type vaporizer 21 is combined side by side by a plurality of vertical installations forms, two adjacent 22 gaps of leaving circulation of air of heat exchanging fin tube, heat exchanging fin tube 22 is connected and is communicated successively by bridge piece 23.Vaporizer 2 of the present invention adopts air temperature type vaporizer 21, air temperature type vaporizer 21 is mainly that the cryogenic media of horizontal tank tank 1 output is become to gas at normal temperature for rear end equipment after air heat exchange, air temperature type vaporizer 21 by with atmosphere in the middle of air generation heat exchange, thereby heating cryogenic media, therefore this vaporizer, without extra thermal source, can be saved other heating agent.
In embodiment, as shown in Figure 3 and Figure 6, what the flow process of unloading of the present invention was included as horizontal tank tank 1 inner container 11 topping ups fills interface 411, this fills interface 411 and through top liquid inlet pipe 412 and bottom liquid inlet pipe 413, is connected with top feed liquor interface 1b and bottom liquid entering hole 1c that horizontal tank tank 1 is shaped with respectively, top feed liquor operating valve 41a is installed on top liquid inlet pipe 412, bottom feed liquor operating valve 41b is installed on bottom liquid inlet pipe 413.
In embodiment, the supercharging flow process comprises that the upper pressure inlet 421 of the upper automatic pressure intensifier 31 of an end connection is connected the lower pressure inlet 422 of lower automatic pressure intensifier 32 with an end, and supercharging gas phase operation valve 42a is installed in the pipeline of upper pressure inlet 421, boost pressure regulation operating valve 42b and supercharging liquid phase operating valve 42c are installed in the pipeline of lower pressure inlet 422 successively, the other end of upper pressure inlet 421 is connected with the upper supercharging interface of connection horizontal tank tank 1 inner container 11 that horizontal tank tank 1 is shaped with, the other end of lower pressure inlet 422 is connected with horizontal tank tank 1 bottom liquid entering hole 1c, and upper automatic pressure intensifier 31 and 32 of lower automatic pressure intensifiers are connected with pressure-equalizing pipe 33.Pressurized machine of the present invention is mainly that horizontal tank tank 1 is carried out to supercharging, and to improve the pressure in horizontal tank tank 1, thereby the gas pressure after gasifying promotes, to meet the use of rear end pressure.
In embodiment, please continue referring to Fig. 3 and Fig. 6, vaporization air feed flow process of the present invention mainly comprises liquid outlet and the liquid transport pipeline 431 between air temperature type vaporizer 21 vaporization imports and the supply air line 432 that is arranged on air temperature type vaporizer 21 air feed ports be communicated with horizontal tank tank 1 is shaped with, on liquid transport pipeline 431, between air temperature type vaporizer 21 vaporization imports, liquid output function valve 43a and emergency cut-off operating valve 43b are installed successively by horizontal tank tank 1 liquid outlet, gas output function valve 43c is installed on supply air line 432.
Safety of the present invention is diffused flow process and is mainly comprised the bulk storage pipeline 44 that is provided with concentrated bulk storage mouth 441, on this bulk storage pipeline 44 and horizontal tank tank 1, set up respectively between the supercharging interface inner core safety anti-explosive pipe-line system and manual blowdown piping are arranged, manually in blowdown piping, manual emptying manipulation valve 44a is installed, inner core safety anti-explosive pipe-line system comprises the first explosion-proof pipeline and the second explosion-proof pipeline of installing side by side through three-way switch valve 44f, the first inner core rupture disk 44b and the first inner core safety valve 44c are installed in the first explosion-proof pipeline, the second inner core rupture disk 44d and the second inner core safety valve 44e are installed in the second explosion-proof pipeline.
In embodiment, one end of bulk storage pipeline 44 is arranged on blowdown valve 44g, before on supply air line 432, being positioned at gas output function valve 43c, setting up air feed raffinate loop and the air feed safety dumping loop all communicated with bulk storage pipeline 44 arranged respectively, air feed residual liquid discharge valve 43d is installed on air feed raffinate loop, steam line safety valve 43e is installed on air feed safety dumping loop, before on liquid transport pipeline 431, being positioned at emergency cut-off operating valve 43b and after liquid output function valve 43a, setting up the pressure regulation pipeline that is communicated with supercharging interface on horizontal tank tank 1 is arranged, reduction regulation operating valve 43f and economic open valve 43g are installed on this pressure regulation pipeline successively.
In embodiment, on the ear end face of horizontal tank tank 1, have gas phase interface and liquid phase interface, the gas phase interface is equipped with gas phase pipe 451, the liquid phase interface is equipped with liquid-phase tube 452, gas phase pipe 451 and liquid-phase tube 452 are connected through level meter equilibrium valve 45a, and level meter gas valve 45b is installed in gas phase pipe 451, level meter liquid phase valve 45c is installed in liquid-phase tube 452, the gas phase connecting end of level meter equilibrium valve 45a and liquid phase connecting end are drawn respectively pressure gauge P and level meter L are installed, horizontal tank tank 1 is fitted with relief valve 6, and fill interface 411 places be equipped with bulk storage pipeline 44, communicate fill residual liquid discharge valve 41c.
In embodiment, framework 9 is long cube structure, and the bight of framework 9 all adopts the container-type corner fittings to connect, horizontal tank tank 1 is in fixed saddle 8 is fixed in framework 9, the front end of framework 9 is equipped with operating valve protective door 91, operating valve protective door 91 is two-door laterally opened, horizontal tank tank 1 is equipped with surveys full packages 7, the supercharging safety line communicated with bulk storage pipeline 44 is installed on upper pressure inlet 421 between supercharging gas phase operation valve 42a and automatic pressure intensifier 31, on this supercharging safety line, is fitted with pressure pipeline safety valve 42d.Framework 9 of the present invention is for square steeel tube is welded to form, and bight adopts the container-type corner fittings not only to be beneficial to carrying, also plays the use of mainly fastening solid and support simultaneously, safe and reliable.The present invention integrates the unloading of traditional blowing model, supercharging, gasification, safety and diffuses; systematic operation is real all by the valve that concentrates on front end, realizes; operability due to valve; for the misoperation that prevents unrelated person and daily protection; therefore framework 9 is provided with operating valve protective door 91; operating valve protective door 91 is double-open type, can open protective door to both sides, is beneficial to operated valve.
Claims (10)
1. integrated storage tank supercharging gasification sledge, comprise that double layer construction is be used to storing the horizontal tank tank (1) of cryogenic media, it is characterized in that: the rear end of described horizontal tank tank (1) is provided with the vaporizer (2) of the interior cryogenic media vaporization of horizontal tank tank (1) being convenient to air feed, the both wings below of this horizontal tank tank (1) is respectively arranged with carries out upper automatic pressure intensifier (31) and the lower automatic pressure intensifier (32) of supercharging to horizontal tank tank (1) from upper and lower two sides, the front end of described horizontal tank tank (1) is provided with operated valve system (4), described operated valve system (4) comprises the flow process of unloading of horizontal tank tank at least, the vaporization air feed flow process that supercharging flow process and safety are diffused flow process and vaporizer, described horizontal tank tank (1), vaporizer (2), upper automatic pressure intensifier (31), lower automatic pressure intensifier (32) and operated valve system (4) are fixedly mounted in the framework (9) that profile meets the standardised container size and form a kind of storage tank supercharging type gasification sledge that storage, supercharging, gasification are structure as a whole that collects.
2. a kind of integrated storage tank supercharging gasification sledge according to claim 1, it is characterized in that: described horizontal tank tank (1) is comprised of inner container (11) and the outer field groove ladle bowl (12) of internal layer, between described groove ladle bowl (12) and inner container (11), be provided with vacuum heat-insulating layer (1a), in this vacuum heat-insulating layer (1a), be filled with pearlife (13), the rear portion of described groove ladle bowl (12) is shaped with urceolus venting (12a), the anti-blasting device (5) of shell is installed on this urceolus venting (12a), and on groove ladle bowl (12), have vacuum orifice (121) and survey vacuum port (122), described vacuum orifice (121) and survey vacuum port (122) are separately installed with vacuum pumping valve (A1) and survey vacuum valve (A2).
3. a kind of integrated storage tank supercharging gasification sledge according to claim 2, it is characterized in that: the air temperature type vaporizer (21) that described vaporizer (2) is heated and carried out cold and hot exchange for air, the heat exchanging fin tube (22) that this air temperature type vaporizer (21) is combined side by side by a plurality of vertical installations forms, between described two adjacent heat exchanging fin tubes (22), leave the gap of circulation of air, described heat exchanging fin tube (22) is connected and is communicated successively by bridge piece (23).
4. a kind of integrated storage tank supercharging gasification sledge according to claim 3, it is characterized in that: what the described flow process of unloading was included as horizontal tank tank (1) inner container (11) topping up fills interface (411), this fills interface (411) and through top liquid inlet pipe (412) and bottom liquid inlet pipe (413), is connected with top feed liquor interface (1b) and bottom liquid entering hole (1c) that horizontal tank tank (1) is shaped with respectively, top feed liquor operating valve (41a) is installed on described top liquid inlet pipe (412), bottom feed liquor operating valve (41b) is installed on described bottom liquid inlet pipe (413).
5. a kind of integrated storage tank supercharging gasification sledge according to claim 4, it is characterized in that: described supercharging flow process comprises that the upper pressure inlet (421) of the upper automatic pressure intensifier (31) of an end connection is connected the lower pressure inlet (422) of lower automatic pressure intensifier (32) with an end, and supercharging gas phase operation valve (42a) is installed in the pipeline of described upper pressure inlet (421), boost pressure regulation operating valve (42b) and supercharging liquid phase operating valve (42c) are installed in the pipeline of described lower pressure inlet (422) successively, the other end of described upper pressure inlet (421) is connected with the upper supercharging interface of connection horizontal tank tank (1) inner container (11) that horizontal tank tank (1) is shaped with, the other end of described lower pressure inlet (422) is connected with horizontal tank tank (1) bottom liquid entering hole (1c), and be connected with pressure-equalizing pipe (33) between described upper automatic pressure intensifier (31) and lower automatic pressure intensifier (32).
6. a kind of integrated storage tank supercharging gasification sledge according to claim 5, it is characterized in that: described vaporization air feed flow process comprises liquid outlet and the liquid transport pipeline (431) between air temperature type vaporizer (21) vaporization import and the supply air line (432) that is arranged on air temperature type vaporizer (21) air feed port be communicated with horizontal tank tank (1) is shaped with, described liquid transport pipeline (431) is upper is equipped with liquid output function valve (43a) and emergency cut-off operating valve (43b) by horizontal tank tank (1) liquid outlet successively between air temperature type vaporizer (21) vaporization import, gas output function valve (43c) is installed on described supply air line (432).
7. a kind of integrated storage tank supercharging gasification sledge according to claim 6, it is characterized in that: described safety is diffused flow process and is comprised the bulk storage pipeline (44) that is provided with concentrated bulk storage mouth (441), between the upper supercharging interface of this bulk storage pipeline (44) and horizontal tank tank (1), set up respectively inner core safety anti-explosive pipe-line system and manual blowdown piping are arranged, manual emptying manipulation valve (44a) is installed in described manual blowdown piping, described inner core safety anti-explosive pipe-line system comprises the first explosion-proof pipeline and the second explosion-proof pipeline of installing side by side through three-way switch valve (44f), the first inner core rupture disk (44b) and the first inner core safety valve (44c) are installed in the described first explosion-proof pipeline, the second inner core rupture disk (44d) and the second inner core safety valve (44e) are installed in the described second explosion-proof pipeline.
8. a kind of integrated storage tank supercharging gasification sledge according to claim 7, it is characterized in that: an end of described bulk storage pipeline (44) is arranged on blowdown valve (44g), on described supply air line (432), be positioned at the front foundation respectively of gas output function valve (43c) air feed raffinate loop and the air feed safety dumping loop all communicated with bulk storage pipeline (44) arranged, described air feed raffinate is equipped with air feed residual liquid discharge valve (43d) on loop, described air feed safety dumping is equipped with steam line safety valve (43e) on loop, on described liquid transport pipeline (431), being positioned at emergency cut-off operating valve (43b) sets up afterwards the pressure regulation pipeline that is communicated with the upper supercharging interface of horizontal tank tank (1) is arranged with liquid output function valve (43a) before, reduction regulation operating valve (43f) and economic open valve (43g) are installed on this pressure regulation pipeline successively.
9. a kind of integrated storage tank supercharging gasification sledge according to claim 8, it is characterized in that: described horizontal tank tank (1) has gas phase interface and liquid phase interface, described gas phase interface is equipped with gas phase pipe (451), described liquid phase interface is equipped with liquid-phase tube (452), described gas phase pipe (451) and liquid-phase tube (452) are connected through level meter equilibrium valve (45a), and level meter gas valve (45b) is installed in described gas phase pipe (451), level meter liquid phase valve (45c) is installed in described liquid-phase tube (452), the gas phase connecting end of described level meter equilibrium valve (45a) and liquid phase connecting end are drawn respectively pressure gauge (P) and level meter (L) are installed, described horizontal tank tank (1) is fitted with relief valve (6), and described fill interface (411) locate to be equipped with bulk storage pipeline (44), communicate fill residual liquid discharge valve (41c).
10. a kind of integrated storage tank supercharging gasification sledge according to claim 9, it is characterized in that: described framework (9) is long cube structure, and the bight of framework (9) all adopts the container-type corner fittings to connect, described horizontal tank tank (1) is in fixed saddle (8) is fixed in framework (9), the front end of described framework (9) is equipped with operating valve protective door (91), described operating valve protective door (91) is two-door laterally opened, described horizontal tank tank (1) is equipped with surveys full packages (7), on described upper pressure inlet (421), be positioned between supercharging gas phase operation valve (42a) and automatic pressure intensifier (31) the supercharging safety line communicated with bulk storage pipeline (44) is installed, on this supercharging safety line, be fitted with pressure pipeline safety valve (42d).
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| CN105737632A (en) * | 2016-04-21 | 2016-07-06 | 珠海市伟名发展有限公司 | Tank type air-temperature vaporizer |
| CN108087724A (en) * | 2017-12-21 | 2018-05-29 | 四川港通医疗设备集团股份有限公司 | A kind of liquid gas storage tank supply line and liquid gas switching method |
| CN108167638A (en) * | 2017-12-20 | 2018-06-15 | 查特深冷工程系统(常州)有限公司 | Cryogenic liquid tank case peculiar to vessel and its operating method |
| CN109654371A (en) * | 2019-01-31 | 2019-04-19 | 陕西融科低温设备有限公司 | A kind of intelligence super-low liquid unloading unit and processand |
| CN109707999A (en) * | 2019-01-31 | 2019-05-03 | 陕西融科低温设备有限公司 | A kind of multi-arm intelligence super-low liquid unloading unit and processand |
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| CN108087724B (en) * | 2017-12-21 | 2023-10-27 | 四川港通医疗设备集团股份有限公司 | Liquefied gas storage tank supply pipeline and liquid-gas switching method |
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| CN109654371B (en) * | 2019-01-31 | 2023-06-16 | 陕西融科低温设备有限公司 | Intelligent ultralow-temperature liquid unloading device and unloading process |
| CN109707999B (en) * | 2019-01-31 | 2023-10-31 | 陕西融科低温设备有限公司 | Multi-arm intelligent ultralow-temperature liquid unloading device and unloading process |
| CN110217500A (en) * | 2019-07-18 | 2019-09-10 | 中车长江车辆有限公司 | Concentrate tapping equipment, gas phase pipeline arranging structure and tank container |
| CN110217500B (en) * | 2019-07-18 | 2024-03-26 | 中车长江车辆有限公司 | Centralized discharging device, gas phase pipeline arrangement structure and tank container |
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