CN103411128B - Integrated storage tank supercharge and gasification sledge - Google Patents

Integrated storage tank supercharge and gasification sledge Download PDF

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Publication number
CN103411128B
CN103411128B CN201310091833.9A CN201310091833A CN103411128B CN 103411128 B CN103411128 B CN 103411128B CN 201310091833 A CN201310091833 A CN 201310091833A CN 103411128 B CN103411128 B CN 103411128B
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tank
valve
supercharging
pipeline
liquid
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CN103411128A (en
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廖建明
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NINGBO MINGXIN CHEMICAL MACHINERY CO Ltd
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NINGBO MINGXIN CHEMICAL MACHINERY CO Ltd
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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

A kind of integrated storage tank supercharging vaporization sledge
Technical field
The present invention relates to a kind of vaporization storage tank device, specifically a kind of integrated storage tank supercharging vaporization sledge.
Background technique
In recent years, the fast development along with China's economy and the demand to environmental protection and energy saving, the every profession and trade of national economy is increasing for the demand of inflammable gas.And blowing model traditional in prior art is mostly the equipment such as storage tank, vaporizer, adjustment pressure device separately and install in scene, separate one-tenth block between its each equipment.The method of construction and installation is carried out at this scene, not only long construction period, and floor space wide and to basis and field requirement relatively high, be therefore unfavorable for the lifting of enterprises production efficiency and the reduction of cost of production.If moreover need again to plan due to enterprise, its relevant air feed equipment just must re-start layout, and equipment Foundations therebetween, integral layout and construction etc. also will be readjusted, and so not only waste time and energy, are also unfavorable for resuming production fast of enterprise.Therefore, traditional blowing model backwardness, is difficult to the needs meeting Economic Development.
Summary of the invention
Technical problem to be solved by this invention is for above-mentioned prior art present situation, and provides collection storage, supercharging, is vaporizated into one and low to in-site installation environmental requirement, and the integrated storage tank supercharging of the one that floor space is little, easy and simple to handle, Security is high is vaporized sledge.
The present invention solves the problems of the technologies described above adopted technological scheme: a kind of integrated storage tank supercharging vaporization sledge, comprise double layer construction for storing the horizontal tank tank of cryogenic media, the rear end of horizontal tank tank is provided with is convenient to the vaporizer of air feed by cryogenic media vaporization in horizontal tank tank, be respectively arranged with below the both wings of this horizontal tank tank, from both up and down, the upper automatic pressure intensifier of supercharging and lower automatic pressure intensifier carried out to horizontal tank tank, the front end of horizontal tank tank is provided with operated valve system, operated valve system at least comprises the flow process of unloading of horizontal tank tank, supercharging flow process and safety diffuse the vaporization air feed flow process of flow process and vaporizer, horizontal tank tank, vaporizer, upper automatic pressure intensifier, lower automatic pressure intensifier and operated valve system be fixedly mounted in framework that profile meets standardised container size form a kind ofly collect storage, supercharging, the storage tank supercharging type that is vaporizated into integrative-structure vaporize sledge.
For optimizing technique scheme, the measure taked also comprises:
Above-mentioned horizontal tank tank is made up of the inner container of internal layer and outer field groove ladle bowl, vacuum heat-insulating layer is provided with between groove ladle bowl and inner container, pearlife is filled with in this vacuum heat-insulating layer, the rear portion of groove ladle bowl is shaped with urceolus venting, this urceolus venting is provided with the anti-blasting device of shell, and 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, this air temperature type vaporizer is made up of multiple heat exchanging fin tube longitudinally installing Side by side groupings, leave the gap of air circulation between two adjacent heat exchanging fin tubes, heat exchanging fin tube is connected successively by bridge piece and is communicated.
Above-mentioned flow process of unloading comprises and fills interface for horizontal tank tank inner container topping up, this fills the top feed liquor interface that interface is shaped with through top liquid inlet pipe and bottom liquid inlet pipe and horizontal tank tank respectively and is connected with bottom liquid entering hole, top liquid inlet pipe is provided with top feed liquor operating valve, bottom liquid inlet pipe is provided with bottom feed liquor operating valve.
Above-mentioned supercharging flow process comprises upper pressure inlet that one end connects upper automatic pressure intensifier is connected automatic pressure intensifier down lower pressure inlet with one 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 upper supercharging interface of the connection horizontal tank tank inner container that the other end and the horizontal tank tank of upper pressure inlet are shaped with is connected, 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 the liquid transport pipeline between liquid outlet and air temperature type vaporizer vaporization import being communicated with and being shaped with at horizontal tank tank and the supply air line being arranged on air temperature type vaporizer air feed port, liquid transport pipeline is vaporized between import by horizontal tank tank liquid outlet to air temperature type vaporizer liquid output function valve and emergency cut-off operating valve are installed successively, supply air line is provided with gas output function valve.
Above-mentioned safety is diffused flow process and is comprised the bulk storage pipeline being provided with and concentrating bulk storage mouth, this bulk storage pipeline and horizontal tank tank set up inner core safety anti-explosive pipe-line system and manual blowdown piping between supercharging interface respectively, manual emptying manipulation valve is installed in manual blowdown piping, inner core safety anti-explosive pipe-line system comprises the first explosion-proof pipeline and the second explosion-proof pipeline installed side by side through three-way switch valve, 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, the air feed raffinate loop and air feed safety dumping loop that have and all communicate with bulk storage pipeline is set up respectively before supply air line being positioned at gas output function valve, air feed raffinate loop is provided with air feed residual liquid discharge valve, loop is provided with steam line safety valve to air feed safety dumping, having with setting up after liquid output function valve the pressure regulation pipeline being communicated with supercharging interface on horizontal tank tank before liquid transport pipeline being positioned at emergency cut-off operating valve, this pressure regulation pipeline being provided with successively reduction regulation operating valve and economic open valve.
Above-mentioned horizontal tank tank has gas phase interface and liquid phase interface, gas phase interface is provided with gas phase pipe, liquid phase interface is provided with liquid-phase tube, gas phase pipe is connected through level meter equilibrium valve with liquid-phase tube, and level meter gas valve is installed in gas phase pipe, 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 and are provided with pressure gauge and level meter, horizontal tank tank is fitted with relief valve, and fill jointing be provided with spread that pipeline communicates fill residual liquid discharge valve.
Above-mentioned framework is long cube structure, and the bight of framework all adopts container-type corner fittings to connect, horizontal tank tank is fixed in framework through fixed saddle, the front end of framework is provided with operating valve protective door, this operating valve protective door is two-door laterally opened, horizontal tank tank survey full packages is installed, upper pressure inlet is provided with between supercharging gas phase operation valve and automatic pressure intensifier and the supercharging safety line spreading pipeline and communicate, this supercharging safety line is fitted with pressure pipeline safety valve.
Compared with prior art, the present invention mainly contains following advantage:
1, level of integration is high: horizontal tank tank, automatic pressure intensifier, vaporizer, operated valve system, operating valve protective door are all arranged in a standard container framework by the present invention, and framework is standard container size, skid-mounted device is compact structure not only, space availability ratio is high, and attractive in appearance, lifting of being more convenient for, transport and storage.
2, floor space is little: due to the high integration of this skid-mounted device, and all storages, supercharging, vaporization and relevant operation system are all arranged in framework, and its area occupied is relatively little, and the placement being beneficial to equipment is installed.
3, swift to operate: because the operated valve in whole equipment is all arranged in one end in framework, therefore, during operation, only need carry out associative operation to a place, carry out the operation of valve without the need to frequent changes place, can the operating time be saved, and operation is rapidly.
4, mobile sensitive: because this equipment relevant is all integrated in a standard container framework, and framework corner adopts container-type corner fittings, therefore, in the middle of transport and handling process, suitable quick and safe, and lifting cost but can, without the need to frequent lifting.
5, install simply: because the bottom part cloth area of this equipment is wide, over all Integration, for its installation requirement, relatively simple, only need look for a smooth cement court, without the need to carrying out storage tank basis and the basic processing of relevant device, greatly can reduce mounting cost, meanwhile, also quick for installation.
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;
Right TV structure figure when Fig. 3 is Fig. 1 non-fitting operation valve protective door;
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 is wherein: 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, first inner core rupture disk 44b, first inner core safety valve 44c, second inner core rupture disk 44d, 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, the anti-blasting device 5 of shell, relief valve 6, survey full packages 7, fixed saddle 8, framework 9, operating valve protective door 91.
As shown in Figures 1 to 6, one of the present invention integrated storage tank supercharging vaporization sledge, comprise double layer construction for storing the horizontal tank tank 1 of cryogenic media, the rear end of horizontal tank tank 1 is provided with the vaporizer 2 be convenient to for rear end equipment air feed of being vaporized by cryogenic media in horizontal tank tank 1, be respectively arranged with below the both wings of this horizontal tank tank 1, from both up and down, the upper automatic pressure intensifier 31 of upper and lower supercharging and lower automatic pressure intensifier 32 carried out to horizontal tank tank 1, the front end of horizontal tank tank 1 is provided with operated valve system 4, this operated valve system 4 at least comprises the flow process of unloading of horizontal tank tank, supercharging flow process and safety diffuse the vaporization air feed flow process of 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 be fixedly mounted in framework 9 that a profile meets standardised container size form a kind ofly collect storage, supercharging, the storage tank supercharging type that is vaporizated into integrative-structure vaporize sledge.Storage, supercharging, vaporization and operation system are concentrated and are fitted in standard container framework 9 inside by the present invention, the scattered distribution pattern of the system such as change the unloading of traditional blowing model, supercharging, vaporization, safety are diffused, not only integral device quick construction, to basis and field requirement low, and simple and efficient to handle, safety properties is high.Framework 9 boundary dimension meets standardised container size, is convenient to the use moving integrally carrying.Operated valve system 4 concentrates on the front end of framework 9, and convenient operation controls, and can operate without the need to frequently walking about.The present invention has that level of integration is high, floor space is little, movement is sensitive and install feature simple and swift to operate.
For optimizing the structure of this sledge further, in embodiment, as shown in Figure 6, horizontal tank tank 1 is made up of the inner container 11 of internal layer and outer field groove ladle bowl 12, vacuum heat-insulating layer 1a is provided with between groove ladle bowl 12 and inner container 11, pearlife 13 is filled with in this vacuum heat-insulating layer 1a, groove ladle bowl 12 of the present invention is shaped with pearlife feeding port, fill by pearlife feeding port, as can see from Figure 1, the rear portion of groove ladle bowl 12 is shaped with urceolus venting 12a, this urceolus venting 12a is provided with the anti-blasting device 5 of shell, and 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.Horizontal tank tank 1 of the present invention mainly plays the use of storage cryogenic media, the Sandwich filling pearlife 13 between groove ladle bowl 12 and inner container 11 vacuumize can better until insulation effect.
In embodiment, as shown in Figure 1, Figure 2 and Figure 4, vaporizer 2 is heated for air and is carried out the air temperature type vaporizer 21 of cold and hot exchange, this air temperature type vaporizer 21 is made up of multiple heat exchanging fin tube 22 longitudinally installing Side by side groupings, leave the gap of air circulation between two adjacent heat exchanging fin tubes 22, heat exchanging fin tube 22 is connected successively by bridge piece 23 and is communicated.Vaporizer 2 of the present invention adopts air temperature type vaporizer 21, the cryogenic media that horizontal tank tank 1 exports mainly is become gas at normal temperature for rear end equipment by air temperature type vaporizer 21 after air heat exchange, air temperature type vaporizer 21 by with air in the middle of air generation heat exchange, thus heating cryogenic media, therefore this vaporizer is without the need to extra thermal source, can save other heating agent.
In embodiment, as shown in Figure 3 and Figure 6, flow process of unloading of the present invention comprises and fills interface 411 for horizontal tank tank 1 inner container 11 topping up, this fills interface 411 and is connected with bottom liquid entering hole 1c through the top feed liquor interface 1b that top liquid inlet pipe 412 and bottom liquid inlet pipe 413 and horizontal tank tank 1 are shaped with respectively, top liquid inlet pipe 412 is provided with top feed liquor operating valve 41a, bottom liquid inlet pipe 413 is provided with bottom feed liquor operating valve 41b.
In embodiment, supercharging flow process comprises upper pressure inlet 421 that one end connects upper automatic pressure intensifier 31 is connected automatic pressure intensifier 32 down lower pressure inlet 422 with one 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 is installed in the pipeline of lower pressure inlet 422 successively, the upper supercharging interface of connection horizontal tank tank 1 inner container 11 that the other end and the horizontal tank tank 1 of upper pressure inlet 421 are shaped with is connected, the other end of 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 upper automatic pressure intensifier 31 and lower automatic pressure intensifier 32.Pressurized machine of the present invention mainly carries out supercharging to horizontal tank tank 1, to improve the pressure in horizontal tank tank 1, thus is promoted by the gas pressure after vaporization, to meet the use of rear end pressure.
In embodiment, please continue see Fig. 3 and Fig. 6, vaporization air feed flow process of the present invention mainly comprises the liquid outlet that is communicated with and is shaped with at horizontal tank tank 1 and air temperature type vaporizer 21 and to vaporize the liquid transport pipeline 431 between import and be arranged on the supply air line 432 of air temperature type vaporizer 21 air feed port, liquid transport pipeline 431 is vaporized between import by horizontal tank tank 1 liquid outlet to air temperature type vaporizer 21 liquid output function valve 43a and emergency cut-off operating valve 43b is installed successively, supply air line 432 is provided with gas output function valve 43c.
Safety of the present invention is diffused flow process and is mainly comprised the bulk storage pipeline 44 being provided with and concentrating bulk storage mouth 441, this bulk storage pipeline 44 and horizontal tank tank 1 set up inner core safety anti-explosive pipe-line system and manual blowdown piping between supercharging interface respectively, manual emptying manipulation valve 44a is installed in manual blowdown piping, inner core safety anti-explosive pipe-line system comprises the first explosion-proof pipeline and the second explosion-proof pipeline installed side by side through three-way switch valve 44f, first inner core rupture disk 44b and the first inner core safety valve 44c is installed in the first explosion-proof pipeline, second inner core rupture disk 44d and the second inner core safety valve 44e is installed in the second explosion-proof pipeline.
In embodiment, one end of bulk storage pipeline 44 is arranged on blowdown valve 44g, the air feed raffinate loop and air feed safety dumping loop that have and all communicate with bulk storage pipeline 44 is set up respectively before supply air line 432 being positioned at gas output function valve 43c, air feed raffinate loop is provided with air feed residual liquid discharge valve 43d, air feed safety dumping loop is provided with steam line safety valve 43e, have with setting up after liquid output function valve 43a the pressure regulation pipeline being communicated with supercharging interface on horizontal tank tank 1 before liquid transport pipeline 431 being positioned at emergency cut-off operating valve 43b, this pressure regulation pipeline is provided with successively reduction regulation operating valve 43f and economic open valve 43g.
In embodiment, the ear end face of horizontal tank tank 1 has gas phase interface and liquid phase interface, gas phase interface is provided with gas phase pipe 451, liquid phase interface is provided with liquid-phase tube 452, gas phase pipe 451 is connected through level meter equilibrium valve 45a with liquid-phase tube 452, 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 and are provided with pressure gauge P and level meter L, horizontal tank tank 1 is fitted with relief valve 6, and fill interface 411 place be provided with spread that pipeline 44 communicates fill residual liquid discharge valve 41c.
In embodiment, framework 9 is long cube structure, and the bight of framework 9 all adopts container-type corner fittings to connect, horizontal tank tank 1 is fixed in framework 9 through fixed saddle 8, the front end of framework 9 is provided with operating valve protective door 91, operating valve protective door 91 is two-door laterally opened, horizontal tank tank 1 is provided with surveys full packages 7, upper pressure inlet 421 is provided with between supercharging gas phase operation valve 42a and automatic pressure intensifier 31 and the supercharging safety line spreading pipeline 44 and communicate, this supercharging safety line is fitted with pressure pipeline safety valve 42d.Framework 9 of the present invention is welded to form for square steeel tube, and bight adopts container-type corner fittings to be not only 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, vaporization, safety are diffused; systematic operation is real is all realized by the valve concentrating on front end; due to the operability of valve; for preventing the misoperation of 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, be beneficial to operated valve to both sides.

Claims (9)

1. an integrated storage tank supercharging vaporization sledge, comprise double layer construction for 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) interior for horizontal tank tank (1) cryogenic media vaporization being convenient to air feed, the upper automatic pressure intensifier (31) and the lower automatic pressure intensifier (32) that from both up and down, horizontal tank tank (1) are carried out to supercharging is respectively arranged with below the both wings of this horizontal tank tank (1), the front end of described horizontal tank tank (1) is provided with operated valve system (4), described operated valve system (4) at least comprises the flow process of unloading of horizontal tank tank, supercharging flow process and safety diffuse the vaporization air feed flow process of 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) be fixedly mounted in framework (9) that profile meets standardised container size form a kind ofly collect storage, supercharging, the storage tank supercharging type that is vaporizated into integrative-structure vaporize sledge, described supercharging flow process comprises upper pressure inlet (421) that one end connects upper automatic pressure intensifier (31) is connected automatic pressure intensifier (32) down lower pressure inlet (422) with one end, and in the pipeline of described upper pressure inlet (421), supercharging gas phase operation valve (42a) is installed, 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 upper supercharging interface of connection horizontal tank tank (1) inner container (11) that the other end and the horizontal tank tank (1) of described upper pressure inlet (421) are shaped with is connected, 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).
2. one according to claim 1 integrated storage tank supercharging vaporization sledge, it is characterized in that: described horizontal tank tank (1) is made up of the inner container (11) of internal layer and outer field groove ladle bowl (12), vacuum heat-insulating layer (1a) is provided with between described groove ladle bowl (12) and inner container (11), pearlife (13) is filled with in this vacuum heat-insulating layer (1a), the rear portion of described groove ladle bowl (12) is shaped with urceolus venting (12a), this urceolus venting (12a) is provided with the anti-blasting device of shell (5), and 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. one according to claim 2 integrated storage tank supercharging vaporization sledge, it is characterized in that: described vaporizer (2) to be heated the air temperature type vaporizer (21) carrying out cold and hot exchange for air, this air temperature type vaporizer (21) is made up of multiple heat exchanging fin tube (22) longitudinally installing Side by side groupings, leave the gap of air circulation between described two adjacent heat exchanging fin tubes (22), described heat exchanging fin tube (22) is connected successively by bridge piece (23) and is communicated.
4. one according to claim 3 integrated storage tank supercharging vaporization sledge, it is characterized in that: described flow process of unloading comprises and fills interface (411) for horizontal tank tank (1) inner container (11) topping up, this fills top feed liquor interface (1b) that interface (411) is shaped with through top liquid inlet pipe (412) and bottom liquid inlet pipe (413) and horizontal tank tank (1) respectively and is connected with bottom liquid entering hole (1c), described top liquid inlet pipe (412) is provided with top feed liquor operating valve (41a), described bottom liquid inlet pipe (413) is provided with bottom feed liquor operating valve (41b).
5. one according to claim 4 integrated storage tank supercharging vaporization sledge, it is characterized in that: described vaporization air feed flow process comprises the liquid transport pipeline (431) between liquid outlet and air temperature type vaporizer (21) vaporization import being communicated with and being shaped with at horizontal tank tank (1) and the supply air line (432) being arranged on air temperature type vaporizer (21) air feed port, described liquid transport pipeline (431) is vaporized between import by horizontal tank tank (1) liquid outlet to air temperature type vaporizer (21) liquid output function valve (43a) and emergency cut-off operating valve (43b) are installed successively, described supply air line (432) is provided with gas output function valve (43c).
6. one according to claim 5 integrated storage tank supercharging vaporization sledge, it is characterized in that: described safety is diffused flow process and comprised the bulk storage pipeline (44) being provided with and concentrating bulk storage mouth (441), inner core safety anti-explosive pipe-line system and manual blowdown piping is set up respectively between this bulk storage pipeline (44) and the upper supercharging interface of horizontal tank tank (1), 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 installed side by side through three-way switch valve (44f), first inner core rupture disk (44b) and the first inner core safety valve (44c) are installed in the described first explosion-proof pipeline, second inner core rupture disk (44d) and the second inner core safety valve (44e) are installed in the described second explosion-proof pipeline.
7. one according to claim 6 integrated storage tank supercharging vaporization sledge, it is characterized in that: one end of described bulk storage pipeline (44) is arranged on blowdown valve (44g), described supply air line (432) is positioned at the front foundation respectively of gas output function valve (43c) and has the air feed raffinate loop and air feed safety dumping loop that all communicate with bulk storage pipeline (44), described air feed raffinate loop is provided with air feed residual liquid discharge valve (43d), described air feed safety dumping loop is provided with steam line safety valve (43e), there is the pressure regulation pipeline being communicated with the upper supercharging interface of horizontal tank tank (1) with foundation after liquid output function valve (43a) before described liquid transport pipeline (431) being positioned at emergency cut-off operating valve (43b), this pressure regulation pipeline is provided with successively reduction regulation operating valve (43f) and economic open valve (43g).
8. one according to claim 7 integrated storage tank supercharging vaporization sledge, it is characterized in that: described horizontal tank tank (1) has gas phase interface and liquid phase interface, described gas phase interface is provided with gas phase pipe (451), described liquid phase interface is provided with liquid-phase tube (452), described gas phase pipe (451) is connected through level meter equilibrium valve (45a) with liquid-phase tube (452), and in described gas phase pipe (451), level meter gas valve (45b) is installed, 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 and are provided with pressure gauge (P) and level meter (L), described horizontal tank tank (1) is fitted with relief valve (6), and described fill interface (411) place be provided with spread that pipeline (44) communicates fill residual liquid discharge valve (41c).
9. one according to claim 8 integrated storage tank supercharging vaporization sledge, it is characterized in that: described framework (9) is long cube structure, and the bight of framework (9) all adopts container-type corner fittings to connect, described horizontal tank tank (1) is fixed in framework (9) through fixed saddle (8), the front end of described framework (9) is provided with operating valve protective door (91), described operating valve protective door (91) is for two-door laterally opened, described horizontal tank tank (1) is provided with surveys full packages (7), described upper pressure inlet (421) is positioned at the supercharging safety line being provided with between supercharging gas phase operation valve (42a) and automatic pressure intensifier (31) with spreading pipeline (44) and communicate, this supercharging safety line is fitted with pressure pipeline safety valve (42d).
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