US2020362861A1PendingUtilityA1
Compressor
Est. expiryJan 12, 2038(~11.5 yrs left)· nominal 20-yr term from priority
F04C 2240/51F04C 2240/30F04C 25/02F04C 29/04F04C 18/16F04C 2240/20F05B 2210/14F04C 2220/12
49
PatentIndex Score
0
Cited by
0
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0
Claims
Abstract
A dry-compressing compressor comprises two screw rotors in a housing defining a suction chamber. At a compressor inlet of the compressor preferably atmospheric pressure prevails and at a compressor outlet of the compressor preferably a pressure of more than 2 bars (absolute) prevails. For each screw rotor at least one displacement element including a helical recess defining a plurality of windings is provided. The at least one displacement element per screw rotor has a single-pass asymmetrical profile.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A dry-compressing compressor comprising
a housing defining a suction chamber and having a compressor inlet where preferably atmospheric pressure prevails and a compressor outlet where preferably a pressure of at least 2 bars (absolute), preferably at least 5 bars (absolute) prevails, two screw rotors arranged in the suction chamber and each having at least one displacement element including a helical recess for defining a plurality of windings, wherein at least one displacement element per screw rotor has a single-pass asymmetrical profile, the screw rotors have no internal cooling of the rotors, and the housing has a mean heat flow density of less than 80000 W/m 2 in the area of the displacement elements.
2 . The dry-compressing compressor according to claim 1 , wherein the profiles are configured such that not blowhole is formed.
3 . The dry-compressing compressor according to claim 1 , wherein the profiles of the at least one displacement element of each screw rotor are configured a Quimby profile.
4 . The dry-compressing compressor according to claim 1 , wherein a displacement element arranged near the outlet of the vacuum pump has symmetrical profile.
5 . The dry-compressing compressor according to claim 1 , wherein at least one displacement element per screw rotor and/or in the case of a plurality of displacement elements per screw rotor said displacement elements jointly comprise a number (n) of windings which is larger than the ratio of outlet pressure (p out ) to inlet pressure (p in ) such that
n
>
Pout
Pin
preferably
n
>
Pout
Pin
+
4.
applies
.
6 . The dry-compressing compressor according to claim 1 , wherein the installed volume ratio between the delivery volume of the inlet stage (V in ) and the outlet stage (V out ) is adapted to the pressure ratio between inlet pressure (p in ) and outlet pressure (p out ) such that the following applies:
V
i
=
Vin
Vout
=
(
Pout
Pin
)
1
/
k
wherein n has a value of k−0.3 to k+0.3 and k is the isotropic exponent of the gas mixture to be delivered.
7 . The dry-compressing compressor according to claim 1 , wherein the displacement elements include at least one area where the volume of the inlet stage (V in ) decreases to a precompression volume (V VK ) in a small rotation angle range, wherein the ratio between inlet volume (V in ) and the volume of the precompression (V VK ) is related to the internal volume ratio (v i ) of the compressor
v
VK
=
Vin
Vout
=
(
v
i
)
1
/
j
wherein j=2 to 5.
8 . The dry-compressing compressor according to claim 7 , wherein the compression from the inlet volume (V in ) to the precompression volume (V VK ) takes place during one and a half to three rotor revolutions (windings).
9 . The dry-compressing compressor according to claim 1 , wherein at least one displacement element per screw rotor and/or in the case of a plurality of displacement elements per screw rotor said displacement elements jointly have a ratio of length (L) to diameter (D) for which the following applies
L
D
>
Pout
2
Pin
-
2
and
in
particular
L
D
>
Pout
2
Pin
-
1
10 . The dry-compressing compressor according to claim 1 , wherein the pitch of the windings of the displacement elements varies, preferably changes and particularly preferably decreases from the compressor inlet to the compressor outlet.
11 . The dry-compressing compressor according to claim 1 , wherein the head and the foot diameter of the rotor preferably continuously changes, wherein the rotor is in particular of a conical configuration.
12 . The dry-compressing compressor according to claim 1 , wherein the pressure ratio
Pout
Pin
between outlet and inlet pressure is at least 5.
13 . The dry-compressing compressor according to claim 1 , wherein two screw rotors with parallel axes are provided.
14 . The dry-compressing compressor according to claim 1 , wherein at the compressor inlet in particular inside the housing a gas collection chamber is provided.
15 . The dry-compressing compressor according to claim 1 , wherein at the compressor outlet a gas collection chamber is provided in particular inside the housing.
16 . The dry-compressing compressor according to claim 1 , wherein in the housing roller bearings and preferably seals are arranged on both sides of the two screw rotors.
17 . The dry-compressing compressor according to claim 1 , wherein for synchronizing the two screw rotors a synchronization gear is provided.
18 . The dry-compressing compressor according to claim 1 , wherein the speed of the screw rotors is higher than
3
,
000
1
min
,
1
min
,
1
min
.
19 . The dry-compressing compressor according to claim 1 , wherein the one displacement element is configured as a discharge-side displacement element and for each screw rotor at least one further displacement element is provided.
20 . The dry-compressing compressor according to claim 1 , wherein between an upper surface of the displacement element and an inner surface of the suction chamber a gap with a height of 0.03 mm to 0.2 mm is formed.
21 . The dry-compressing compressor according to claim 1 , wherein the suction-side displacement elements have a constant pitch along their overall length.
22 . The dry-compressing compressor according to claim 1 , wherein each screw rotor comprises a rotor shaft supporting the at least one displacement element.
23 . The dry-compressing compressor according to claim 1 , wherein the displacement elements of a screw rotor are of an integral configuration.
24 . The dry-compressing compressor according to claim 1 , wherein the screw rotors and in particular the at least one displacement element per screw rotor have a smaller expansion coefficient that the housing, wherein the expansion coefficient of the housing is in particular at least larger than that of the screw rotors and/or the at least one displacement element.
25 . The dry-compressing compressor according to claim 1 , wherein the screw rotors do not comprise any ducts through which in particular a liquid coolant flows.
26 . The dry-compressing compressor according to claim 1 , wherein the screw rotors are of a solid configuration.
27 . The dry-compressing compressor according to claim 1 , wherein a temperature difference in the area of the discharge-side displacement elements between the latter and the housing during normal operation is smaller than 50 K.
28 . The dry-compressing compressor according to claim 1 , wherein the distance between the area where 5 ° A) to 20% of the outlet pressure prevails and the last winding of the discharge-side displacement element is at least 20% to 30% of the rotor length.
29 . The dry-compressing compressor according to claim 1 , wherein a gap between the edges of at least one of the displacement elements preferably has a gap height of 0.1 to 0.3 mm.Cited by (0)
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